/*---------------------------------------------------------------------------*\ | ========= | | | \\ / F ield | OpenFOAM: The Open Source CFD Toolbox | | \\ / O peration | Version: 2.2.x | | \\ / A nd | Web: www.OpenFOAM.org | | \\/ M anipulation | | \*---------------------------------------------------------------------------*/ Build : 2.2.x-b477bcabd47f Exec : sprayEngineFoam Date : May 08 2013 Time : 16:39:37 Host : "tolkien01" PID : 31243 Case : /home/gandalf/FOAMCases/sprayEngineFoam nProcs : 1 sigFpe : Enabling floating point exception trapping (FOAM_SIGFPE). fileModificationChecking : Monitoring run-time modified files using timeStampMaster allowSystemOperations : Allowing user-supplied system call operations // * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * // Create engine time Create mesh for time = -180 Selecting engineMesh layered deckHeight: 0.1 piston position: 0 Reading g Creating combustion model Selecting combustion model PaSR Selecting chemistry type { chemistrySolver ode; chemistryThermo psi; } Selecting thermodynamics package { type hePsiThermo; mixture reactingMixture; transport sutherland; thermo janaf; energy sensibleEnthalpy; equationOfState perfectGas; specie specie; } Selecting chemistryReader chemkinReader Reading CHEMKIN thermo data in new file format chemistryModel: Number of species = 5 and reactions = 1 Selecting ODE solver SIBS Creating component thermo properties: multi-component carrier - 5 species liquids - 1 components solids - 0 components Reading field U Reading/calculating face flux field phi Creating turbulence model Selecting turbulence model type RASModel Selecting RAS turbulence model RNGkEpsilon RNGkEpsilonCoeffs { Cmu 0.0845; C1 1.42; C2 1.68; C3 -0.33; sigmak 0.71942; sigmaEps 0.71942; Prt 1; eta0 4.38; beta 0.012; } Creating field dpdt Creating field kinetic energy K No finite volume options present Constructing reacting cloud Constructing particle forces Selecting particle force sphereDrag Constructing cloud functions none Constructing particle injection models Creating injector: model1 Selecting injection model coneNozzleInjection Constructing 3-D injection Selecting distribution model RosinRammler Selecting dispersion model none Selecting patch interaction model standardWallInteraction Selecting surface film model none Selecting U integration scheme Euler Selecting heat transfer model RanzMarshall Selecting T integration scheme analytical Selecting composition model singlePhaseMixture Selecting phase change model liquidEvaporationBoil Participating liquid species: C7H16 Selecting AtomizationModel none Selecting BreakupModel ReitzDiwakar Selecting StochasticCollisionModel none Average parcel mass: 2.3999e-11 Radiation model not active: radiationProperties not found Selecting radiationModel none Courant Number mean: 0 max: 0 Total cylinder mass: 0.00143268 PIMPLE: Operating solver in PISO mode Starting time loop Courant Number mean: 0 max: 0 deltaT = 1.19995e-06 Crank angle = -179.999 CA-deg deltaZ = 5.42741e-12 clearance: 0.1 Piston speed = 4.52302e-06 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 1, Final residual = 8.84376e-07, No Iterations 1 DILUPBiCG: Solving for Uy, Initial residual = 1, Final residual = 8.83115e-07, No Iterations 1 DILUPBiCG: Solving for Uz, Initial residual = 1, Final residual = 1.06549e-06, No Iterations 1 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 8.83416e-05, Final residual = 1.77777e-10, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 1, Final residual = 1.395e-06, No Iterations 1 T gas min/max = 373, 433 DICPCG: Solving for p, Initial residual = 1, Final residual = 0.00201463, No Iterations 1 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.58177e-09, global = 1.30987e-09, cumulative = 1.30987e-09 DICPCG: Solving for p, Initial residual = 0.000767213, Final residual = 1.01988e-08, No Iterations 2 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.35969e-14, global = -1.68854e-14, cumulative = 1.30985e-09 DILUPBiCG: Solving for epsilon, Initial residual = 0.000945119, Final residual = 2.05386e-09, No Iterations 1 DILUPBiCG: Solving for k, Initial residual = 1, Final residual = 3.50162e-06, No Iterations 1 Mean pressure:100000 Mean temperature:373 Mean u':1.63283 ExecutionTime = 27.48 s ClockTime = 28 s Courant Number mean: 5.61936e-08 max: 1.62784e-06 deltaT = 1.4398e-06 Crank angle = -179.997 CA-deg deltaZ = 2.08385e-11 clearance: 0.1 Piston speed = 1.44732e-05 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.374973, Final residual = 2.96978e-07, No Iterations 1 DILUPBiCG: Solving for Uy, Initial residual = 0.374973, Final residual = 2.96555e-07, No Iterations 1 DILUPBiCG: Solving for Uz, Initial residual = 0.375038, Final residual = 5.04733e-07, No Iterations 1 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 9.58927e-05, Final residual = 2.42783e-10, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.346032, Final residual = 3.41501e-07, No Iterations 1 T gas min/max = 373, 433 DICPCG: Solving for p, Initial residual = 0.34669, Final residual = 0.00129958, No Iterations 1 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.52841e-09, global = 3.22052e-09, cumulative = 4.53037e-09 DICPCG: Solving for p, Initial residual = 0.000846294, Final residual = 3.79789e-08, No Iterations 2 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.12932e-13, global = -1.42039e-13, cumulative = 4.53022e-09 DILUPBiCG: Solving for epsilon, Initial residual = 0.000654693, Final residual = 2.31409e-09, No Iterations 1 DILUPBiCG: Solving for k, Initial residual = 0.703963, Final residual = 2.99717e-06, No Iterations 1 Mean pressure:100000 Mean temperature:373.001 Mean u':1.63264 ExecutionTime = 45.62 s ClockTime = 46 s Courant Number mean: 2.5046e-07 max: 6.72943e-06 deltaT = 1.72747e-06 Crank angle = -179.996 CA-deg deltaZ = 4.56253e-11 clearance: 0.1 Piston speed = 2.64117e-05 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.304627, Final residual = 3.6456e-07, No Iterations 1 DILUPBiCG: Solving for Uy, Initial residual = 0.304627, Final residual = 3.64272e-07, No Iterations 1 DILUPBiCG: Solving for Uz, Initial residual = 0.311089, Final residual = 6.01751e-07, No Iterations 1 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 9.94067e-05, Final residual = 6.43277e-10, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.211967, Final residual = 3.03548e-07, No Iterations 1 T gas min/max = 373, 433 DICPCG: Solving for p, Initial residual = 0.216644, Final residual = 0.00116652, No Iterations 1 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 8.28722e-09, global = 4.95751e-09, cumulative = 9.48773e-09 DICPCG: Solving for p, Initial residual = 0.000886179, Final residual = 1.24175e-07, No Iterations 2 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.20474e-12, global = -7.43168e-13, cumulative = 9.48699e-09 DILUPBiCG: Solving for epsilon, Initial residual = 0.000767646, Final residual = 3.89747e-09, No Iterations 1 DILUPBiCG: Solving for k, Initial residual = 0.564629, Final residual = 3.43802e-06, No Iterations 1 Mean pressure:100000 Mean temperature:373.001 Mean u':1.63241 ExecutionTime = 59.15 s ClockTime = 60 s Courant Number mean: 6.69348e-07 max: 1.59569e-05 deltaT = 2.07296e-06 Crank angle = -179.994 CA-deg deltaZ = 8.44457e-11 clearance: 0.1 Piston speed = 4.07368e-05 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.252899, Final residual = 4.69269e-07, No Iterations 1 DILUPBiCG: Solving for Uy, Initial residual = 0.252899, Final residual = 4.68761e-07, No Iterations 1 DILUPBiCG: Solving for Uz, Initial residual = 0.26947, Final residual = 7.49247e-07, No Iterations 1 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 9.98665e-05, Final residual = 5.06021e-10, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.158354, Final residual = 3.35268e-07, No Iterations 1 T gas min/max = 373, 433 DICPCG: Solving for p, Initial residual = 0.163726, Final residual = 0.00131463, No Iterations 1 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.5068e-08, global = 8.23542e-09, cumulative = 1.77224e-08 DICPCG: Solving for p, Initial residual = 0.00106338, Final residual = 4.34793e-07, No Iterations 2 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 6.31753e-12, global = -2.86221e-12, cumulative = 1.77196e-08 DILUPBiCG: Solving for epsilon, Initial residual = 0.000898565, Final residual = 6.55525e-09, No Iterations 1 DILUPBiCG: Solving for k, Initial residual = 0.484854, Final residual = 4.21931e-06, No Iterations 1 Mean pressure:100001 Mean temperature:373.002 Mean u':1.63213 ExecutionTime = 72.65 s ClockTime = 73 s Courant Number mean: 1.42575e-06 max: 2.88199e-05 deltaT = 2.48693e-06 Crank angle = -179.991 CA-deg deltaZ = 1.44054e-10 clearance: 0.1 Piston speed = 5.79246e-05 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.211552, Final residual = 5.76515e-07, No Iterations 1 DILUPBiCG: Solving for Uy, Initial residual = 0.211552, Final residual = 5.7595e-07, No Iterations 1 DILUPBiCG: Solving for Uz, Initial residual = 0.240911, Final residual = 9.62086e-07, No Iterations 1 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 9.34296e-05, Final residual = 6.60591e-10, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.13122, Final residual = 4.18283e-07, No Iterations 1 T gas min/max = 373, 433 DICPCG: Solving for p, Initial residual = 0.143106, Final residual = 0.00226128, No Iterations 1 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.74227e-08, global = 2.19595e-08, cumulative = 3.9679e-08 DICPCG: Solving for p, Initial residual = 0.00192269, Final residual = 5.18455e-08, No Iterations 3 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.03351e-12, global = -4.11865e-14, cumulative = 3.9679e-08 DILUPBiCG: Solving for epsilon, Initial residual = 0.00104957, Final residual = 1.09908e-08, No Iterations 1 DILUPBiCG: Solving for k, Initial residual = 0.433533, Final residual = 5.38278e-06, No Iterations 1 Mean pressure:100001 Mean temperature:373.003 Mean u':1.6318 ExecutionTime = 86.04 s ClockTime = 87 s Courant Number mean: 2.66577e-06 max: 4.28415e-05 deltaT = 2.98343e-06 Crank angle = -179.988 CA-deg deltaZ = 2.34331e-10 clearance: 0.1 Piston speed = 7.85442e-05 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.177743, Final residual = 6.35123e-07, No Iterations 1 DILUPBiCG: Solving for Uy, Initial residual = 0.177743, Final residual = 6.34483e-07, No Iterations 1 DILUPBiCG: Solving for Uz, Initial residual = 0.220425, Final residual = 1.26376e-06, No Iterations 1 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 9.70102e-05, Final residual = 1.13e-09, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.115517, Final residual = 5.6251e-07, No Iterations 1 T gas min/max = 373, 433 DICPCG: Solving for p, Initial residual = 0.141635, Final residual = 0.00334038, No Iterations 1 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 7.43892e-08, global = 4.64428e-08, cumulative = 8.61217e-08 DICPCG: Solving for p, Initial residual = 0.00295185, Final residual = 3.1121e-07, No Iterations 3 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 8.08981e-12, global = -8.60134e-13, cumulative = 8.61209e-08 DILUPBiCG: Solving for epsilon, Initial residual = 0.00122239, Final residual = 1.83798e-08, No Iterations 1 DILUPBiCG: Solving for k, Initial residual = 0.376554, Final residual = 6.66224e-06, No Iterations 1 Mean pressure:100001 Mean temperature:373.004 Mean u':1.6314 ExecutionTime = 99.55 s ClockTime = 100 s Courant Number mean: 4.58757e-06 max: 5.54491e-05 deltaT = 3.5784e-06 Crank angle = -179.985 CA-deg deltaZ = 3.6957e-10 clearance: 0.1 Piston speed = 0.000103278 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.151285, Final residual = 7.32819e-07, No Iterations 1 DILUPBiCG: Solving for Uy, Initial residual = 0.151285, Final residual = 7.3238e-07, No Iterations 1 DILUPBiCG: Solving for Uz, Initial residual = 0.205024, Final residual = 1.68679e-06, No Iterations 1 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 9.66446e-05, Final residual = 1.77516e-09, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.106132, Final residual = 7.88798e-07, No Iterations 1 T gas min/max = 373, 433 DICPCG: Solving for p, Initial residual = 0.128479, Final residual = 0.00452937, No Iterations 1 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.29644e-07, global = 8.0519e-08, cumulative = 1.6664e-07 DICPCG: Solving for p, Initial residual = 0.00417776, Final residual = 1.05558e-07, No Iterations 4 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.43749e-12, global = 5.9492e-13, cumulative = 1.6664e-07 DILUPBiCG: Solving for epsilon, Initial residual = 0.00141838, Final residual = 3.06475e-08, No Iterations 1 DILUPBiCG: Solving for k, Initial residual = 0.338458, Final residual = 8.52093e-06, No Iterations 1 Mean pressure:100001 Mean temperature:373.005 Mean u':1.63093 ExecutionTime = 113.05 s ClockTime = 114 s Courant Number mean: 7.47469e-06 max: 6.73539e-05 deltaT = 4.29346e-06 Crank angle = -179.98 CA-deg deltaZ = 5.70815e-10 clearance: 0.1 Piston speed = 0.00013295 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.132561, Final residual = 9.61862e-07, No Iterations 1 DILUPBiCG: Solving for Uy, Initial residual = 0.132561, Final residual = 9.61248e-07, No Iterations 1 DILUPBiCG: Solving for Uz, Initial residual = 0.192942, Final residual = 2.27906e-06, No Iterations 1 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000100805, Final residual = 2.16611e-09, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.100514, Final residual = 1.12219e-06, No Iterations 1 T gas min/max = 373, 433 DICPCG: Solving for p, Initial residual = 0.121306, Final residual = 0.00657431, No Iterations 1 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.33101e-07, global = 1.34943e-07, cumulative = 3.01583e-07 DICPCG: Solving for p, Initial residual = 0.00616397, Final residual = 6.64585e-07, No Iterations 4 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.6216e-11, global = 1.26949e-12, cumulative = 3.01584e-07 DILUPBiCG: Solving for epsilon, Initial residual = 0.00164063, Final residual = 5.09847e-08, No Iterations 1 DILUPBiCG: Solving for k, Initial residual = 0.312441, Final residual = 6.35514e-10, No Iterations 2 Mean pressure:100002 Mean temperature:373.007 Mean u':1.63036 ExecutionTime = 126.47 s ClockTime = 127 s Courant Number mean: 1.17538e-05 max: 8.15003e-05 deltaT = 5.15038e-06 Crank angle = -179.975 CA-deg deltaZ = 8.6808e-10 clearance: 0.1 Piston speed = 0.000168547 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.12213, Final residual = 1.4072e-06, No Iterations 1 DILUPBiCG: Solving for Uy, Initial residual = 0.12213, Final residual = 1.40589e-06, No Iterations 1 DILUPBiCG: Solving for Uz, Initial residual = 0.182814, Final residual = 3.09883e-06, No Iterations 1 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 9.14346e-05, Final residual = 2.79471e-09, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0973718, Final residual = 1.60505e-06, No Iterations 1 T gas min/max = 373, 433 DICPCG: Solving for p, Initial residual = 0.120461, Final residual = 0.0099415, No Iterations 1 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.22931e-07, global = 2.25144e-07, cumulative = 5.26728e-07 DICPCG: Solving for p, Initial residual = 0.00948222, Final residual = 5.54536e-07, No Iterations 5 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.5682e-11, global = 2.69168e-12, cumulative = 5.26731e-07 DILUPBiCG: Solving for epsilon, Initial residual = 0.0018906, Final residual = 8.44643e-08, No Iterations 1 DILUPBiCG: Solving for k, Initial residual = 0.293709, Final residual = 1.21599e-09, No Iterations 2 Mean pressure:100002 Mean temperature:373.008 Mean u':1.62967 ExecutionTime = 139.95 s ClockTime = 141 s Courant Number mean: 1.80436e-05 max: 9.87466e-05 deltaT = 6.17279e-06 Crank angle = -179.969 CA-deg deltaZ = 1.30386e-09 clearance: 0.1 Piston speed = 0.000211228 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.11553, Final residual = 2.03593e-06, No Iterations 1 DILUPBiCG: Solving for Uy, Initial residual = 0.11553, Final residual = 2.03301e-06, No Iterations 1 DILUPBiCG: Solving for Uz, Initial residual = 0.173627, Final residual = 4.21616e-06, No Iterations 1 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 9.88569e-05, Final residual = 5.17932e-09, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0959262, Final residual = 2.32096e-06, No Iterations 1 T gas min/max = 373, 433 DICPCG: Solving for p, Initial residual = 0.123079, Final residual = 0.00224585, No Iterations 2 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.11126e-07, global = 2.7334e-08, cumulative = 5.54065e-07 DICPCG: Solving for p, Initial residual = 0.00218428, Final residual = 8.05073e-07, No Iterations 5 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.24371e-11, global = -1.20978e-11, cumulative = 5.54053e-07 DILUPBiCG: Solving for epsilon, Initial residual = 0.00216817, Final residual = 1.39003e-07, No Iterations 1 DILUPBiCG: Solving for k, Initial residual = 0.279591, Final residual = 2.33661e-09, No Iterations 2 Mean pressure:100003 Mean temperature:373.01 Mean u':1.62885 ExecutionTime = 153.5 s ClockTime = 154 s Courant Number mean: 2.72208e-05 max: 0.000119434 deltaT = 7.40551e-06 Crank angle = -179.961 CA-deg deltaZ = 1.94327e-09 clearance: 0.1 Piston speed = 0.000262409 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.109624, Final residual = 3.03941e-06, No Iterations 1 DILUPBiCG: Solving for Uy, Initial residual = 0.109624, Final residual = 3.03464e-06, No Iterations 1 DILUPBiCG: Solving for Uz, Initial residual = 0.164875, Final residual = 5.74972e-06, No Iterations 1 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 9.7403e-05, Final residual = 6.96906e-08, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0949585, Final residual = 3.40456e-06, No Iterations 1 T gas min/max = 373, 433 DICPCG: Solving for p, Initial residual = 0.12906, Final residual = 0.00428452, No Iterations 2 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.38865e-07, global = 5.89826e-08, cumulative = 6.13035e-07 DICPCG: Solving for p, Initial residual = 0.00420526, Final residual = 3.04779e-07, No Iterations 7 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.76148e-11, global = -2.82765e-12, cumulative = 6.13033e-07 DILUPBiCG: Solving for epsilon, Initial residual = 0.00247775, Final residual = 2.28325e-07, No Iterations 1 DILUPBiCG: Solving for k, Initial residual = 0.269154, Final residual = 4.53336e-09, No Iterations 2 Mean pressure:100003 Mean temperature:373.013 Mean u':1.62787 ExecutionTime = 167.09 s ClockTime = 168 s Courant Number mean: 4.05581e-05 max: 0.000145871 deltaT = 8.87601e-06 Crank angle = -179.953 CA-deg deltaZ = 2.87387e-09 clearance: 0.1 Piston speed = 0.000323779 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.104473, Final residual = 4.75521e-06, No Iterations 1 DILUPBiCG: Solving for Uy, Initial residual = 0.104473, Final residual = 4.75007e-06, No Iterations 1 DILUPBiCG: Solving for Uz, Initial residual = 0.155577, Final residual = 7.82982e-06, No Iterations 1 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000102555, Final residual = 2.72937e-08, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0936398, Final residual = 5.02463e-06, No Iterations 1 T gas min/max = 373, 433 DICPCG: Solving for p, Initial residual = 0.140068, Final residual = 0.00822022, No Iterations 2 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.98493e-07, global = 1.09199e-07, cumulative = 7.22231e-07 DICPCG: Solving for p, Initial residual = 0.00832709, Final residual = 8.11442e-07, No Iterations 8 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.92899e-11, global = -6.62983e-12, cumulative = 7.22225e-07 DILUPBiCG: Solving for epsilon, Initial residual = 0.00281601, Final residual = 3.72045e-07, No Iterations 1 DILUPBiCG: Solving for k, Initial residual = 0.260808, Final residual = 8.76843e-09, No Iterations 2 Mean pressure:100004 Mean temperature:373.016 Mean u':1.6267 ExecutionTime = 180.66 s ClockTime = 181 s Courant Number mean: 5.9616e-05 max: 0.000179707 deltaT = 1.06284e-05 Crank angle = -179.942 CA-deg deltaZ = 4.22262e-09 clearance: 0.1 Piston speed = 0.000397298 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0997416, Final residual = 7.63704e-06, No Iterations 1 DILUPBiCG: Solving for Uy, Initial residual = 0.0997419, Final residual = 7.63595e-06, No Iterations 1 DILUPBiCG: Solving for Uz, Initial residual = 0.145214, Final residual = 2.37546e-09, No Iterations 2 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 9.32422e-05, Final residual = 1.09226e-08, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0927546, Final residual = 7.50345e-06, No Iterations 1 T gas min/max = 373, 433 DICPCG: Solving for p, Initial residual = 0.158808, Final residual = 0.00683289, No Iterations 3 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.32768e-07, global = 1.44351e-08, cumulative = 7.3666e-07 DICPCG: Solving for p, Initial residual = 0.00683572, Final residual = 7.11693e-07, No Iterations 9 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.36533e-11, global = -8.89651e-12, cumulative = 7.36651e-07 DILUPBiCG: Solving for epsilon, Initial residual = 0.00318615, Final residual = 6.02147e-07, No Iterations 1 DILUPBiCG: Solving for k, Initial residual = 0.253897, Final residual = 1.68701e-08, No Iterations 2 Mean pressure:100005 Mean temperature:373.019 Mean u':1.6253 ExecutionTime = 194.27 s ClockTime = 195 s Courant Number mean: 8.63034e-05 max: 0.000222508 deltaT = 1.27376e-05 Crank angle = -179.929 CA-deg deltaZ = 6.18247e-09 clearance: 0.1 Piston speed = 0.000485372 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0951037, Final residual = 3.80934e-09, No Iterations 2 DILUPBiCG: Solving for Uy, Initial residual = 0.0951034, Final residual = 3.7087e-09, No Iterations 2 DILUPBiCG: Solving for Uz, Initial residual = 0.133542, Final residual = 4.42144e-09, No Iterations 2 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000102469, Final residual = 1.85341e-08, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0924367, Final residual = 1.88211e-09, No Iterations 2 T gas min/max = 373, 433 DICPCG: Solving for p, Initial residual = 0.188473, Final residual = 0.0130311, No Iterations 3 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 8.31045e-07, global = 3.62001e-08, cumulative = 7.72851e-07 DICPCG: Solving for p, Initial residual = 0.0138381, Final residual = 9.26765e-07, No Iterations 11 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.5421e-11, global = -9.39585e-12, cumulative = 7.72841e-07 DILUPBiCG: Solving for epsilon, Initial residual = 0.00359684, Final residual = 9.73376e-07, No Iterations 1 DILUPBiCG: Solving for k, Initial residual = 0.248712, Final residual = 3.25509e-08, No Iterations 2 Mean pressure:100006 Mean temperature:373.024 Mean u':1.62362 ExecutionTime = 207.99 s ClockTime = 209 s Courant Number mean: 0.000122558 max: 0.000278136 deltaT = 1.52614e-05 Crank angle = -179.914 CA-deg deltaZ = 9.01814e-09 clearance: 0.1 Piston speed = 0.00059091 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0899824, Final residual = 9.04101e-09, No Iterations 2 DILUPBiCG: Solving for Uy, Initial residual = 0.0899816, Final residual = 9.02206e-09, No Iterations 2 DILUPBiCG: Solving for Uz, Initial residual = 0.119812, Final residual = 7.87555e-09, No Iterations 2 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000101039, Final residual = 6.11689e-08, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0924361, Final residual = 4.3585e-09, No Iterations 2 T gas min/max = 373, 433 DICPCG: Solving for p, Initial residual = 0.229596, Final residual = 0.0211522, No Iterations 3 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.31645e-06, global = 5.91485e-08, cumulative = 8.3199e-07 DICPCG: Solving for p, Initial residual = 0.024975, Final residual = 5.98912e-07, No Iterations 14 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.21469e-11, global = -3.78784e-12, cumulative = 8.31986e-07 DILUPBiCG: Solving for epsilon, Initial residual = 0.00404666, Final residual = 1.56598e-06, No Iterations 1 DILUPBiCG: Solving for k, Initial residual = 0.244627, Final residual = 6.25322e-08, No Iterations 2 Mean pressure:100008 Mean temperature:373.029 Mean u':1.62163 ExecutionTime = 221.65 s ClockTime = 223 s Courant Number mean: 0.000168898 max: 0.000347668 deltaT = 1.82683e-05 Crank angle = -179.896 CA-deg deltaZ = 1.31038e-08 clearance: 0.1 Piston speed = 0.000717295 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0840514, Final residual = 1.70027e-08, No Iterations 2 DILUPBiCG: Solving for Uy, Initial residual = 0.0840506, Final residual = 1.73169e-08, No Iterations 2 DILUPBiCG: Solving for Uz, Initial residual = 0.102986, Final residual = 1.33245e-08, No Iterations 2 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000106271, Final residual = 6.81937e-08, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0925303, Final residual = 8.75781e-09, No Iterations 2 T gas min/max = 373.001, 433 DICPCG: Solving for p, Initial residual = 0.296509, Final residual = 0.0230861, No Iterations 4 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.30682e-06, global = 5.06655e-08, cumulative = 8.82652e-07 DICPCG: Solving for p, Initial residual = 0.0294975, Final residual = 7.80712e-07, No Iterations 16 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.41302e-11, global = -1.25925e-12, cumulative = 8.8265e-07 DILUPBiCG: Solving for epsilon, Initial residual = 0.00453426, Final residual = 2.5006e-06, No Iterations 1 DILUPBiCG: Solving for k, Initial residual = 0.241281, Final residual = 1.1895e-07, No Iterations 2 Mean pressure:100009 Mean temperature:373.035 Mean u':1.61925 ExecutionTime = 235.33 s ClockTime = 236 s Courant Number mean: 0.000223279 max: 0.00042367 deltaT = 2.18568e-05 Crank angle = -179.874 CA-deg deltaZ = 1.89835e-08 clearance: 0.0999999 Piston speed = 0.000868541 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0781731, Final residual = 2.20812e-08, No Iterations 2 DILUPBiCG: Solving for Uy, Initial residual = 0.0781727, Final residual = 2.24354e-08, No Iterations 2 DILUPBiCG: Solving for Uz, Initial residual = 0.0807928, Final residual = 2.01789e-08, No Iterations 2 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 9.78313e-05, Final residual = 4.44241e-08, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0926328, Final residual = 1.51128e-08, No Iterations 2 T gas min/max = 373.002, 433 DICPCG: Solving for p, Initial residual = 0.412691, Final residual = 0.0264959, No Iterations 5 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.27713e-06, global = 1.11622e-07, cumulative = 9.94272e-07 DICPCG: Solving for p, Initial residual = 0.0472174, Final residual = 5.87537e-07, No Iterations 20 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.64459e-11, global = 6.94928e-13, cumulative = 9.94273e-07 DILUPBiCG: Solving for epsilon, Initial residual = 0.00506273, Final residual = 3.9618e-06, No Iterations 1 DILUPBiCG: Solving for k, Initial residual = 0.23866, Final residual = 2.23996e-07, No Iterations 2 Mean pressure:100011 Mean temperature:373.042 Mean u':1.61642 ExecutionTime = 249.03 s ClockTime = 250 s Courant Number mean: 0.000279637 max: 0.000495993 deltaT = 2.62046e-05 Crank angle = -179.848 CA-deg deltaZ = 2.7507e-08 clearance: 0.0999999 Piston speed = 0.0010497 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0692442, Final residual = 2.32395e-08, No Iterations 2 DILUPBiCG: Solving for Uy, Initial residual = 0.0692435, Final residual = 2.35232e-08, No Iterations 2 DILUPBiCG: Solving for Uz, Initial residual = 0.0525423, Final residual = 2.52015e-08, No Iterations 2 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000109246, Final residual = 7.86704e-08, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.092888, Final residual = 2.51363e-08, No Iterations 2 T gas min/max = 373.007, 433 DICPCG: Solving for p, Initial residual = 0.612972, Final residual = 0.0519299, No Iterations 6 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.99144e-06, global = 2.24156e-07, cumulative = 1.21843e-06 DICPCG: Solving for p, Initial residual = 0.133444, Final residual = 7.5093e-07, No Iterations 24 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.19093e-11, global = 1.07709e-12, cumulative = 1.21843e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.00564925, Final residual = 6.25151e-06, No Iterations 1 DILUPBiCG: Solving for k, Initial residual = 0.237247, Final residual = 4.21816e-07, No Iterations 2 Mean pressure:100014 Mean temperature:373.05 Mean u':1.61306 ExecutionTime = 262.78 s ClockTime = 264 s Courant Number mean: 0.000325991 max: 0.000546439 deltaT = 3.12765e-05 Crank angle = -179.816 CA-deg deltaZ = 3.96075e-08 clearance: 0.0999999 Piston speed = 0.00126637 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0529594, Final residual = 4.51151e-08, No Iterations 2 DILUPBiCG: Solving for Uy, Initial residual = 0.0529601, Final residual = 4.4151e-08, No Iterations 2 DILUPBiCG: Solving for Uz, Initial residual = 0.0267851, Final residual = 2.44438e-08, No Iterations 2 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000108956, Final residual = 1.09703e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0926195, Final residual = 4.25757e-08, No Iterations 2 T gas min/max = 373.014, 433 DICPCG: Solving for p, Initial residual = 0.758638, Final residual = 0.0479158, No Iterations 7 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.73975e-06, global = 1.76907e-07, cumulative = 1.39534e-06 DICPCG: Solving for p, Initial residual = 0.0705034, Final residual = 7.05006e-07, No Iterations 27 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.9751e-11, global = 2.57251e-12, cumulative = 1.39534e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0062631, Final residual = 9.58088e-06, No Iterations 1 DILUPBiCG: Solving for k, Initial residual = 0.235269, Final residual = 7.69715e-07, No Iterations 2 Mean pressure:100016 Mean temperature:373.061 Mean u':1.60908 ExecutionTime = 276.54 s ClockTime = 278 s Courant Number mean: 0.000341219 max: 0.000538391 deltaT = 3.73378e-05 Crank angle = -179.779 CA-deg deltaZ = 5.69402e-08 clearance: 0.0999998 Piston speed = 0.001525 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0836409, Final residual = 1.53738e-07, No Iterations 2 DILUPBiCG: Solving for Uy, Initial residual = 0.083643, Final residual = 1.52699e-07, No Iterations 2 DILUPBiCG: Solving for Uz, Initial residual = 0.107279, Final residual = 1.8248e-07, No Iterations 2 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000114626, Final residual = 1.53348e-07, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0922079, Final residual = 7.89559e-08, No Iterations 2 T gas min/max = 373.018, 433 DICPCG: Solving for p, Initial residual = 0.677181, Final residual = 0.0550309, No Iterations 7 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.65127e-06, global = -2.42801e-08, cumulative = 1.37106e-06 DICPCG: Solving for p, Initial residual = 0.0711507, Final residual = 9.9696e-07, No Iterations 31 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.88573e-11, global = 1.52417e-12, cumulative = 1.37106e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.00691871, Final residual = 4.11771e-08, No Iterations 2 DILUPBiCG: Solving for k, Initial residual = 0.234045, Final residual = 1.39049e-06, No Iterations 2 Mean pressure:100020 Mean temperature:373.073 Mean u':1.60438 ExecutionTime = 290.33 s ClockTime = 292 s Courant Number mean: 0.000317309 max: 0.000593045 deltaT = 4.46658e-05 Crank angle = -179.734 CA-deg deltaZ = 8.19216e-08 clearance: 0.0999997 Piston speed = 0.0018341 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.199469, Final residual = 5.84163e-07, No Iterations 2 DILUPBiCG: Solving for Uy, Initial residual = 0.199471, Final residual = 5.80228e-07, No Iterations 2 DILUPBiCG: Solving for Uz, Initial residual = 0.202592, Final residual = 6.39866e-07, No Iterations 2 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000106765, Final residual = 1.80871e-07, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0917288, Final residual = 1.53953e-07, No Iterations 2 T gas min/max = 373.022, 433 DICPCG: Solving for p, Initial residual = 0.635321, Final residual = 0.0633802, No Iterations 9 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.86727e-06, global = 1.55952e-07, cumulative = 1.52701e-06 DICPCG: Solving for p, Initial residual = 0.138763, Final residual = 8.58852e-07, No Iterations 38 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.65582e-11, global = 9.23714e-13, cumulative = 1.52701e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.00762368, Final residual = 8.65307e-08, No Iterations 2 DILUPBiCG: Solving for k, Initial residual = 0.233907, Final residual = 2.50393e-06, No Iterations 2 Mean pressure:100023 Mean temperature:373.087 Mean u':1.59883 ExecutionTime = 304.22 s ClockTime = 305 s Courant Number mean: 0.000286337 max: 0.000678394 deltaT = 5.31975e-05 Crank angle = -179.681 CA-deg deltaZ = 1.17193e-07 clearance: 0.0999996 Piston speed = 0.00220298 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.222691, Final residual = 1.2373e-06, No Iterations 2 DILUPBiCG: Solving for Uy, Initial residual = 0.222695, Final residual = 1.23334e-06, No Iterations 2 DILUPBiCG: Solving for Uz, Initial residual = 0.15328, Final residual = 8.98345e-07, No Iterations 2 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000116246, Final residual = 9.15887e-07, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0905835, Final residual = 2.8379e-07, No Iterations 2 T gas min/max = 373.028, 433 DICPCG: Solving for p, Initial residual = 0.755384, Final residual = 0.0680117, No Iterations 11 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.32875e-06, global = 1.66782e-07, cumulative = 1.69379e-06 DICPCG: Solving for p, Initial residual = 0.373341, Final residual = 8.39693e-07, No Iterations 45 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.12318e-11, global = 1.35006e-14, cumulative = 1.69379e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0083268, Final residual = 1.78797e-07, No Iterations 2 DILUPBiCG: Solving for k, Initial residual = 0.23324, Final residual = 4.38834e-06, No Iterations 2 Mean pressure:100028 Mean temperature:373.103 Mean u':1.59231 ExecutionTime = 318.11 s ClockTime = 319 s Courant Number mean: 0.000314282 max: 0.000785097 deltaT = 6.32619e-05 Crank angle = -179.618 CA-deg deltaZ = 1.67136e-07 clearance: 0.0999994 Piston speed = 0.00264197 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0596276, Final residual = 8.35377e-07, No Iterations 2 DILUPBiCG: Solving for Uy, Initial residual = 0.0596336, Final residual = 8.6447e-07, No Iterations 2 DILUPBiCG: Solving for Uz, Initial residual = 0.0488675, Final residual = 5.13223e-07, No Iterations 2 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000118602, Final residual = 3.09086e-07, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0892599, Final residual = 5.04283e-07, No Iterations 2 T gas min/max = 373.035, 433 DICPCG: Solving for p, Initial residual = 0.881067, Final residual = 0.0510381, No Iterations 14 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.13233e-06, global = 3.43821e-08, cumulative = 1.72818e-06 DICPCG: Solving for p, Initial residual = 0.164563, Final residual = 7.2846e-07, No Iterations 47 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.67754e-11, global = 8.92111e-14, cumulative = 1.72818e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.00919343, Final residual = 3.58475e-07, No Iterations 2 DILUPBiCG: Solving for k, Initial residual = 0.232818, Final residual = 7.58145e-06, No Iterations 2 Mean pressure:100033 Mean temperature:373.123 Mean u':1.58469 ExecutionTime = 332.05 s ClockTime = 333 s Courant Number mean: 0.000443671 max: 0.000925759 deltaT = 7.57068e-05 Crank angle = -179.542 CA-deg deltaZ = 2.39673e-07 clearance: 0.0999992 Piston speed = 0.0031658 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.097779, Final residual = 1.6659e-06, No Iterations 2 DILUPBiCG: Solving for Uy, Initial residual = 0.0977771, Final residual = 1.63968e-06, No Iterations 2 DILUPBiCG: Solving for Uz, Initial residual = 0.100298, Final residual = 1.90271e-06, No Iterations 2 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.00012704, Final residual = 5.04533e-07, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0886577, Final residual = 9.18394e-07, No Iterations 2 T gas min/max = 373.04, 433 DICPCG: Solving for p, Initial residual = 0.827868, Final residual = 0.0642054, No Iterations 14 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.97773e-06, global = 5.3702e-09, cumulative = 1.73355e-06 DICPCG: Solving for p, Initial residual = 0.260667, Final residual = 8.5441e-07, No Iterations 55 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.82521e-11, global = 4.08385e-13, cumulative = 1.73355e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0108735, Final residual = 7.88157e-07, No Iterations 2 DILUPBiCG: Solving for k, Initial residual = 0.234319, Final residual = 1.6288e-07, No Iterations 3 Mean pressure:100040 Mean temperature:373.146 Mean u':1.57575 ExecutionTime = 346.05 s ClockTime = 347 s Courant Number mean: 0.000611061 max: 0.00110738 deltaT = 9.08482e-05 Crank angle = -179.451 CA-deg deltaZ = 3.44644e-07 clearance: 0.0999989 Piston speed = 0.00379362 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.077207, Final residual = 2.62947e-06, No Iterations 2 DILUPBiCG: Solving for Uy, Initial residual = 0.0772129, Final residual = 2.61709e-06, No Iterations 2 DILUPBiCG: Solving for Uz, Initial residual = 0.059243, Final residual = 2.00217e-06, No Iterations 2 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000127029, Final residual = 1.31866e-08, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0885275, Final residual = 1.69331e-06, No Iterations 2 T gas min/max = 373.049, 433 DICPCG: Solving for p, Initial residual = 0.855563, Final residual = 0.080133, No Iterations 14 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 7.15425e-06, global = 2.93345e-08, cumulative = 1.76288e-06 DICPCG: Solving for p, Initial residual = 0.483993, Final residual = 9.16692e-07, No Iterations 65 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.65429e-11, global = 2.24834e-14, cumulative = 1.76288e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0138317, Final residual = 1.75332e-06, No Iterations 2 DILUPBiCG: Solving for k, Initial residual = 0.236544, Final residual = 3.60637e-07, No Iterations 3 Mean pressure:100048 Mean temperature:373.174 Mean u':1.56527 ExecutionTime = 360.12 s ClockTime = 362 s Courant Number mean: 0.000708519 max: 0.0012852 deltaT = 0.000108575 Crank angle = -179.343 CA-deg deltaZ = 4.93509e-07 clearance: 0.0999984 Piston speed = 0.00454535 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0246187, Final residual = 1.113e-06, No Iterations 2 DILUPBiCG: Solving for Uy, Initial residual = 0.0246248, Final residual = 1.08734e-06, No Iterations 2 DILUPBiCG: Solving for Uz, Initial residual = 0.0244333, Final residual = 1.36967e-06, No Iterations 2 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000132244, Final residual = 1.31501e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0881692, Final residual = 2.99606e-06, No Iterations 2 T gas min/max = 373.06, 433 DICPCG: Solving for p, Initial residual = 0.905291, Final residual = 0.0781795, No Iterations 16 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 7.81966e-06, global = 9.44512e-09, cumulative = 1.77233e-06 DICPCG: Solving for p, Initial residual = 0.402572, Final residual = 8.69047e-07, No Iterations 71 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.87087e-11, global = 6.20248e-15, cumulative = 1.77233e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0172956, Final residual = 3.60071e-06, No Iterations 2 DILUPBiCG: Solving for k, Initial residual = 0.238192, Final residual = 7.64163e-07, No Iterations 3 Mean pressure:100057 Mean temperature:373.206 Mean u':1.55308 ExecutionTime = 374.23 s ClockTime = 376 s Courant Number mean: 0.000760374 max: 0.00145969 deltaT = 0.000127735 Crank angle = -179.215 CA-deg deltaZ = 6.94384e-07 clearance: 0.0999977 Piston speed = 0.00543613 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0767036, Final residual = 7.68496e-06, No Iterations 2 DILUPBiCG: Solving for Uy, Initial residual = 0.0767018, Final residual = 7.59609e-06, No Iterations 2 DILUPBiCG: Solving for Uz, Initial residual = 0.0367732, Final residual = 3.51895e-06, No Iterations 2 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000133463, Final residual = 4.2909e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0865886, Final residual = 4.8462e-06, No Iterations 2 T gas min/max = 373.071, 433 DICPCG: Solving for p, Initial residual = 0.896795, Final residual = 0.0760174, No Iterations 17 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 8.96248e-06, global = 2.25636e-08, cumulative = 1.79489e-06 DICPCG: Solving for p, Initial residual = 0.450324, Final residual = 8.99877e-07, No Iterations 75 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.13047e-11, global = -3.79877e-15, cumulative = 1.79489e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0211714, Final residual = 6.85118e-06, No Iterations 2 DILUPBiCG: Solving for k, Initial residual = 0.236859, Final residual = 1.46094e-06, No Iterations 3 Mean pressure:100067 Mean temperature:373.243 Mean u':1.53915 ExecutionTime = 388.34 s ClockTime = 390 s Courant Number mean: 0.000850104 max: 0.00164599 deltaT = 0.000150545 Crank angle = -179.065 CA-deg deltaZ = 9.76307e-07 clearance: 0.0999967 Piston speed = 0.00648516 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0339015, Final residual = 6.49983e-06, No Iterations 2 DILUPBiCG: Solving for Uy, Initial residual = 0.033939, Final residual = 6.53979e-06, No Iterations 2 DILUPBiCG: Solving for Uz, Initial residual = 0.0449932, Final residual = 7.07003e-06, No Iterations 2 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000145017, Final residual = 5.96907e-08, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.085499, Final residual = 7.8444e-06, No Iterations 2 T gas min/max = 373.084, 433 DICPCG: Solving for p, Initial residual = 0.907059, Final residual = 0.0906201, No Iterations 17 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.2379e-05, global = 2.64318e-08, cumulative = 1.82132e-06 DICPCG: Solving for p, Initial residual = 0.501401, Final residual = 9.65124e-07, No Iterations 82 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.82589e-11, global = -1.76887e-14, cumulative = 1.82132e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.026543, Final residual = 3.42732e-07, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.236926, Final residual = 2.74686e-06, No Iterations 3 Mean pressure:100080 Mean temperature:373.286 Mean u':1.52327 ExecutionTime = 402.55 s ClockTime = 404 s Courant Number mean: 0.000987784 max: 0.00189809 deltaT = 0.000176726 Crank angle = -178.888 CA-deg deltaZ = 1.36414e-06 clearance: 0.0999953 Piston speed = 0.00771892 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.020264, Final residual = 4.66149e-06, No Iterations 2 DILUPBiCG: Solving for Uy, Initial residual = 0.0202205, Final residual = 4.72381e-06, No Iterations 2 DILUPBiCG: Solving for Uz, Initial residual = 0.047164, Final residual = 3.13859e-07, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000154628, Final residual = 9.89941e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0844391, Final residual = 3.06339e-07, No Iterations 3 T gas min/max = 373.099, 433 DICPCG: Solving for p, Initial residual = 0.907638, Final residual = 0.0811433, No Iterations 18 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.29646e-05, global = 2.54972e-08, cumulative = 1.84682e-06 DICPCG: Solving for p, Initial residual = 0.453294, Final residual = 8.26769e-07, No Iterations 86 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.83185e-11, global = 1.76563e-14, cumulative = 1.84682e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0340474, Final residual = 7.58764e-07, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.236828, Final residual = 4.93445e-06, No Iterations 3 Mean pressure:100094 Mean temperature:373.335 Mean u':1.50531 ExecutionTime = 416.81 s ClockTime = 419 s Courant Number mean: 0.00112287 max: 0.0021877 deltaT = 0.000204631 Crank angle = -178.683 CA-deg deltaZ = 1.87373e-06 clearance: 0.0999935 Piston speed = 0.00915665 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0261883, Final residual = 3.51302e-07, No Iterations 3 DILUPBiCG: Solving for Uy, Initial residual = 0.0262037, Final residual = 3.56377e-07, No Iterations 3 DILUPBiCG: Solving for Uz, Initial residual = 0.0480383, Final residual = 5.65302e-07, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000165233, Final residual = 6.56545e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0827017, Final residual = 5.43611e-07, No Iterations 3 T gas min/max = 373.117, 433 DICPCG: Solving for p, Initial residual = 0.906362, Final residual = 0.0900529, No Iterations 19 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.66872e-05, global = 3.56975e-08, cumulative = 1.88252e-06 DICPCG: Solving for p, Initial residual = 0.523341, Final residual = 9.61883e-07, No Iterations 89 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.65617e-11, global = 4.27605e-14, cumulative = 1.88252e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0426831, Final residual = 1.5463e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.234486, Final residual = 8.12047e-06, No Iterations 3 Mean pressure:100111 Mean temperature:373.391 Mean u':1.48534 ExecutionTime = 431.14 s ClockTime = 433 s Courant Number mean: 0.00124826 max: 0.00248173 deltaT = 0.000230209 Crank angle = -178.453 CA-deg deltaZ = 2.48537e-06 clearance: 0.099991 Piston speed = 0.0107961 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0317789, Final residual = 6.34311e-07, No Iterations 3 DILUPBiCG: Solving for Uy, Initial residual = 0.0317677, Final residual = 6.53653e-07, No Iterations 3 DILUPBiCG: Solving for Uz, Initial residual = 0.0530859, Final residual = 9.75406e-07, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000166165, Final residual = 1.87895e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0793265, Final residual = 8.26261e-07, No Iterations 3 T gas min/max = 373.137, 433 DICPCG: Solving for p, Initial residual = 0.912504, Final residual = 0.0767756, No Iterations 20 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.59626e-05, global = 4.84788e-08, cumulative = 1.931e-06 DICPCG: Solving for p, Initial residual = 0.455533, Final residual = 7.25091e-07, No Iterations 94 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.15824e-11, global = 1.89011e-14, cumulative = 1.931e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0517204, Final residual = 2.72834e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.227111, Final residual = 5.69558e-07, No Iterations 4 Mean pressure:100130 Mean temperature:373.453 Mean u':1.46381 ExecutionTime = 445.46 s ClockTime = 447 s Courant Number mean: 0.00135485 max: 0.0027399 deltaT = 0.000265626 Crank angle = -178.187 CA-deg deltaZ = 3.36436e-06 clearance: 0.0999876 Piston speed = 0.0126658 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0369715, Final residual = 1.19008e-06, No Iterations 3 DILUPBiCG: Solving for Uy, Initial residual = 0.0368548, Final residual = 1.21285e-06, No Iterations 3 DILUPBiCG: Solving for Uz, Initial residual = 0.0630209, Final residual = 1.85817e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000177144, Final residual = 5.21182e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0786942, Final residual = 1.41249e-06, No Iterations 3 T gas min/max = 373.16, 433 DICPCG: Solving for p, Initial residual = 0.907679, Final residual = 0.0637758, No Iterations 27 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.55141e-05, global = 2.34481e-08, cumulative = 1.95444e-06 DICPCG: Solving for p, Initial residual = 0.382427, Final residual = 9.83878e-07, No Iterations 91 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.06415e-11, global = 1.39802e-14, cumulative = 1.95444e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0631535, Final residual = 5.20862e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.226735, Final residual = 1.06668e-06, No Iterations 4 Mean pressure:100152 Mean temperature:373.523 Mean u':1.44011 ExecutionTime = 459.8 s ClockTime = 462 s Courant Number mean: 0.00151012 max: 0.00308894 deltaT = 0.000318751 Crank angle = -177.869 CA-deg deltaZ = 4.73969e-06 clearance: 0.0999829 Piston speed = 0.0148696 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0368518, Final residual = 1.69889e-06, No Iterations 3 DILUPBiCG: Solving for Uy, Initial residual = 0.0374062, Final residual = 1.64077e-06, No Iterations 3 DILUPBiCG: Solving for Uz, Initial residual = 0.0718528, Final residual = 3.9826e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000187205, Final residual = 4.04867e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0814427, Final residual = 2.85256e-06, No Iterations 3 T gas min/max = 373.188, 433 DICPCG: Solving for p, Initial residual = 0.901117, Final residual = 0.0788655, No Iterations 32 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.35195e-05, global = 2.4327e-08, cumulative = 1.97877e-06 DICPCG: Solving for p, Initial residual = 0.443809, Final residual = 8.90311e-07, No Iterations 96 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.90386e-11, global = -8.58082e-15, cumulative = 1.97877e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0786437, Final residual = 8.37476e-07, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.234914, Final residual = 2.38886e-06, No Iterations 4 Mean pressure:100179 Mean temperature:373.607 Mean u':1.41316 ExecutionTime = 474.22 s ClockTime = 476 s Courant Number mean: 0.00175299 max: 0.00363834 deltaT = 0.000358595 Crank angle = -177.51 CA-deg deltaZ = 6.24832e-06 clearance: 0.0999766 Piston speed = 0.0174244 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.034857, Final residual = 2.30462e-06, No Iterations 3 DILUPBiCG: Solving for Uy, Initial residual = 0.0349329, Final residual = 2.34059e-06, No Iterations 3 DILUPBiCG: Solving for Uz, Initial residual = 0.0758348, Final residual = 6.2849e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000193718, Final residual = 5.17616e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0793387, Final residual = 4.21348e-06, No Iterations 3 T gas min/max = 373.22, 433 DICPCG: Solving for p, Initial residual = 0.900797, Final residual = 0.0885075, No Iterations 28 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.03002e-05, global = 6.44946e-08, cumulative = 2.04327e-06 DICPCG: Solving for p, Initial residual = 0.483386, Final residual = 8.66912e-07, No Iterations 97 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 7.00103e-11, global = -6.72314e-15, cumulative = 2.04327e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0933136, Final residual = 1.56588e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.229278, Final residual = 3.7065e-06, No Iterations 4 Mean pressure:100210 Mean temperature:373.699 Mean u':1.38448 ExecutionTime = 488.66 s ClockTime = 491 s Courant Number mean: 0.00190822 max: 0.00399281 deltaT = 0.000418361 Crank angle = -177.092 CA-deg deltaZ = 8.51606e-06 clearance: 0.0999681 Piston speed = 0.0203557 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0688891, Final residual = 1.10622e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.0687405, Final residual = 1.0463e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0834832, Final residual = 7.65523e-07, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000210168, Final residual = 3.28747e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0807809, Final residual = 7.25713e-06, No Iterations 3 T gas min/max = 373.258, 433 DICPCG: Solving for p, Initial residual = 0.895662, Final residual = 0.0825466, No Iterations 36 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.40415e-05, global = 2.02148e-08, cumulative = 2.06348e-06 DICPCG: Solving for p, Initial residual = 0.450447, Final residual = 9.337e-07, No Iterations 102 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 9.36013e-11, global = 2.97121e-14, cumulative = 2.06348e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.112499, Final residual = 3.36304e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.231979, Final residual = 6.7474e-06, No Iterations 4 Mean pressure:100247 Mean temperature:373.806 Mean u':1.35305 ExecutionTime = 503.23 s ClockTime = 505 s Courant Number mean: 0.00215797 max: 0.00454863 deltaT = 0.000418361 Crank angle = -176.673 CA-deg deltaZ = 9.83715e-06 clearance: 0.0999583 Piston speed = 0.0235135 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0408972, Final residual = 7.78419e-06, No Iterations 3 DILUPBiCG: Solving for Uy, Initial residual = 0.0410631, Final residual = 7.4826e-06, No Iterations 3 DILUPBiCG: Solving for Uz, Initial residual = 0.0786803, Final residual = 7.07838e-07, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000205564, Final residual = 6.52313e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0714698, Final residual = 6.39398e-06, No Iterations 3 T gas min/max = 373.297, 433 DICPCG: Solving for p, Initial residual = 0.902437, Final residual = 0.0742931, No Iterations 36 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.13902e-05, global = 1.41501e-08, cumulative = 2.07763e-06 DICPCG: Solving for p, Initial residual = 0.428313, Final residual = 7.47524e-07, No Iterations 98 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 7.34369e-11, global = -5.6095e-16, cumulative = 2.07763e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.122933, Final residual = 3.54248e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.20538, Final residual = 5.8107e-06, No Iterations 4 Mean pressure:100285 Mean temperature:373.913 Mean u':1.32329 ExecutionTime = 517.71 s ClockTime = 520 s Courant Number mean: 0.00210389 max: 0.00446592 deltaT = 0.000418361 Crank angle = -176.255 CA-deg deltaZ = 1.11588e-05 clearance: 0.0999471 Piston speed = 0.0266725 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.043584, Final residual = 5.90494e-06, No Iterations 3 DILUPBiCG: Solving for Uy, Initial residual = 0.0446288, Final residual = 6.75945e-06, No Iterations 3 DILUPBiCG: Solving for Uz, Initial residual = 0.0800789, Final residual = 9.80254e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.00020473, Final residual = 9.74764e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0645391, Final residual = 5.72177e-06, No Iterations 3 T gas min/max = 373.337, 433 DICPCG: Solving for p, Initial residual = 0.905432, Final residual = 0.0776196, No Iterations 35 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.38231e-05, global = 2.08285e-08, cumulative = 2.09846e-06 DICPCG: Solving for p, Initial residual = 0.449738, Final residual = 9.44304e-07, No Iterations 101 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 9.20596e-11, global = 6.19959e-15, cumulative = 2.09846e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.132912, Final residual = 3.69137e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.184676, Final residual = 5.06913e-06, No Iterations 4 Mean pressure:100325 Mean temperature:374.02 Mean u':1.29505 ExecutionTime = 532.22 s ClockTime = 534 s Courant Number mean: 0.00205761 max: 0.00435901 deltaT = 0.000418361 Crank angle = -175.837 CA-deg deltaZ = 1.24809e-05 clearance: 0.0999346 Piston speed = 0.0298329 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0486457, Final residual = 7.7236e-06, No Iterations 3 DILUPBiCG: Solving for Uy, Initial residual = 0.0485546, Final residual = 7.75667e-06, No Iterations 3 DILUPBiCG: Solving for Uz, Initial residual = 0.0747425, Final residual = 8.9324e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000204891, Final residual = 6.692e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0591537, Final residual = 5.19296e-06, No Iterations 3 T gas min/max = 373.378, 433 DICPCG: Solving for p, Initial residual = 0.906308, Final residual = 0.0787645, No Iterations 37 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.54982e-05, global = 1.28485e-08, cumulative = 2.11131e-06 DICPCG: Solving for p, Initial residual = 0.46344, Final residual = 9.96389e-07, No Iterations 103 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 9.93178e-11, global = 1.04723e-15, cumulative = 2.11131e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.142747, Final residual = 3.83973e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.168051, Final residual = 4.47232e-06, No Iterations 4 Mean pressure:100366 Mean temperature:374.127 Mean u':1.2682 ExecutionTime = 546.74 s ClockTime = 549 s Courant Number mean: 0.00201845 max: 0.00429349 deltaT = 0.000418361 Crank angle = -175.418 CA-deg deltaZ = 1.38037e-05 clearance: 0.0999208 Piston speed = 0.0329947 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0416305, Final residual = 5.37153e-06, No Iterations 3 DILUPBiCG: Solving for Uy, Initial residual = 0.0438512, Final residual = 6.53574e-06, No Iterations 3 DILUPBiCG: Solving for Uz, Initial residual = 0.0717921, Final residual = 8.19719e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000205587, Final residual = 7.50364e-08, No Iterations 3 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0548415, Final residual = 4.76224e-06, No Iterations 3 T gas min/max = 373.421, 433 DICPCG: Solving for p, Initial residual = 0.909071, Final residual = 0.0834674, No Iterations 35 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.88213e-05, global = 2.43425e-08, cumulative = 2.13565e-06 DICPCG: Solving for p, Initial residual = 0.486308, Final residual = 7.16029e-07, No Iterations 104 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 7.17258e-11, global = -3.05656e-16, cumulative = 2.13565e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.152465, Final residual = 3.97306e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.154349, Final residual = 3.98337e-06, No Iterations 4 Mean pressure:100408 Mean temperature:374.234 Mean u':1.24261 ExecutionTime = 561.21 s ClockTime = 563 s Courant Number mean: 0.00197895 max: 0.00417751 deltaT = 0.000418361 Crank angle = -175 CA-deg deltaZ = 1.51272e-05 clearance: 0.0999057 Piston speed = 0.0361583 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0534505, Final residual = 8.12245e-06, No Iterations 3 DILUPBiCG: Solving for Uy, Initial residual = 0.0518652, Final residual = 8.61219e-06, No Iterations 3 DILUPBiCG: Solving for Uz, Initial residual = 0.0669493, Final residual = 7.50817e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000201084, Final residual = 5.42058e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0512988, Final residual = 4.40022e-06, No Iterations 3 T gas min/max = 373.466, 433 DICPCG: Solving for p, Initial residual = 0.912015, Final residual = 0.0862692, No Iterations 38 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.13775e-05, global = 1.07283e-08, cumulative = 2.14638e-06 DICPCG: Solving for p, Initial residual = 0.512484, Final residual = 8.28274e-07, No Iterations 103 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 8.61766e-11, global = 4.52962e-15, cumulative = 2.14638e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.161865, Final residual = 4.08324e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.142828, Final residual = 3.57631e-06, No Iterations 4 Mean pressure:100452 Mean temperature:374.342 Mean u':1.21819 ExecutionTime = 577.43 s ClockTime = 586 s Courant Number mean: 0.00194587 max: 0.00413577 deltaT = 0.00050002 Crank angle = -174.5 CA-deg deltaZ = 1.98172e-05 clearance: 0.0998859 Piston speed = 0.0396327 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0444002, Final residual = 1.25728e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.0460272, Final residual = 9.68438e-06, No Iterations 3 DILUPBiCG: Solving for Uz, Initial residual = 0.07525, Final residual = 1.17517e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000223637, Final residual = 8.98574e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0573993, Final residual = 8.80431e-06, No Iterations 3 T gas min/max = 373.521, 433 DICPCG: Solving for p, Initial residual = 0.907678, Final residual = 0.0697735, No Iterations 40 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.16458e-05, global = 4.86834e-09, cumulative = 2.15125e-06 DICPCG: Solving for p, Initial residual = 0.459001, Final residual = 8.11506e-07, No Iterations 105 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.00834e-10, global = 4.91384e-15, cumulative = 2.15125e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.187676, Final residual = 9.0755e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.15576, Final residual = 7.54702e-06, No Iterations 4 Mean pressure:100507 Mean temperature:374.472 Mean u':1.19068 ExecutionTime = 591.88 s ClockTime = 601 s Courant Number mean: 0.00227579 max: 0.00483081 deltaT = 0.000562523 Crank angle = -173.938 CA-deg deltaZ = 2.45573e-05 clearance: 0.0998613 Piston speed = 0.0436556 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0392341, Final residual = 2.06196e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.0369125, Final residual = 2.08726e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0707167, Final residual = 1.73358e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000242409, Final residual = 2.68493e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0602704, Final residual = 9.62288e-07, No Iterations 4 T gas min/max = 373.585, 433 DICPCG: Solving for p, Initial residual = 0.91143, Final residual = 0.088727, No Iterations 38 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 6.17166e-05, global = 1.10017e-08, cumulative = 2.16225e-06 DICPCG: Solving for p, Initial residual = 0.522281, Final residual = 9.65696e-07, No Iterations 106 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.4933e-10, global = -1.49885e-14, cumulative = 2.16225e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.211236, Final residual = 1.6569e-06, No Iterations 5 DILUPBiCG: Solving for k, Initial residual = 0.159753, Final residual = 1.32856e-06, No Iterations 5 Mean pressure:100570 Mean temperature:374.619 Mean u':1.16158 ExecutionTime = 606.47 s ClockTime = 615 s Courant Number mean: 0.00250375 max: 0.00536648 deltaT = 0.000656276 Crank angle = -173.281 CA-deg deltaZ = 3.16814e-05 clearance: 0.0998296 Piston speed = 0.0482745 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0834374, Final residual = 8.13088e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.085707, Final residual = 7.53135e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.08142, Final residual = 3.56639e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000268402, Final residual = 3.13392e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0655724, Final residual = 1.90743e-06, No Iterations 4 T gas min/max = 373.664, 433 DICPCG: Solving for p, Initial residual = 0.907993, Final residual = 0.0631114, No Iterations 42 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.37128e-05, global = 3.35791e-09, cumulative = 2.16561e-06 DICPCG: Solving for p, Initial residual = 0.476051, Final residual = 9.94099e-07, No Iterations 109 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.87753e-10, global = 9.40295e-14, cumulative = 2.16561e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.238123, Final residual = 3.51395e-06, No Iterations 5 DILUPBiCG: Solving for k, Initial residual = 0.168477, Final residual = 2.66031e-06, No Iterations 5 Mean pressure:100648 Mean temperature:374.792 Mean u':1.12995 ExecutionTime = 621.11 s ClockTime = 630 s Courant Number mean: 0.00284858 max: 0.00617723 deltaT = 0.000656276 Crank angle = -172.625 CA-deg deltaZ = 3.49497e-05 clearance: 0.0997947 Piston speed = 0.0532545 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0588062, Final residual = 3.05902e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.0633014, Final residual = 4.7988e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0741063, Final residual = 3.10386e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000256926, Final residual = 2.89486e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0614824, Final residual = 1.74825e-06, No Iterations 4 T gas min/max = 373.745, 433 DICPCG: Solving for p, Initial residual = 0.914782, Final residual = 0.0905533, No Iterations 41 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 8.01323e-05, global = 1.40739e-08, cumulative = 2.17968e-06 DICPCG: Solving for p, Initial residual = 0.572114, Final residual = 7.20281e-07, No Iterations 110 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.53092e-10, global = -6.27934e-14, cumulative = 2.17968e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.250364, Final residual = 3.56968e-06, No Iterations 5 DILUPBiCG: Solving for k, Initial residual = 0.154907, Final residual = 2.34434e-06, No Iterations 5 Mean pressure:100730 Mean temperature:374.966 Mean u':1.10022 ExecutionTime = 635.74 s ClockTime = 644 s Courant Number mean: 0.00277854 max: 0.00591073 deltaT = 0.000656276 Crank angle = -171.969 CA-deg deltaZ = 3.82222e-05 clearance: 0.0997565 Piston speed = 0.0582411 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0933928, Final residual = 1.07957e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.096474, Final residual = 8.68616e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0771595, Final residual = 3.13759e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000263184, Final residual = 2.01542e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0582356, Final residual = 1.62081e-06, No Iterations 4 T gas min/max = 373.831, 433 DICPCG: Solving for p, Initial residual = 0.913279, Final residual = 0.0706947, No Iterations 43 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 6.57457e-05, global = 3.61405e-09, cumulative = 2.18329e-06 DICPCG: Solving for p, Initial residual = 0.502678, Final residual = 7.54332e-07, No Iterations 110 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.61073e-10, global = 1.34864e-13, cumulative = 2.18329e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.261042, Final residual = 3.59655e-06, No Iterations 5 DILUPBiCG: Solving for k, Initial residual = 0.143427, Final residual = 2.08499e-06, No Iterations 5 Mean pressure:100815 Mean temperature:375.142 Mean u':1.07222 ExecutionTime = 650.43 s ClockTime = 659 s Courant Number mean: 0.00271277 max: 0.00592718 deltaT = 0.000656276 Crank angle = -171.312 CA-deg deltaZ = 4.14996e-05 clearance: 0.099715 Piston speed = 0.0632349 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0670908, Final residual = 4.69416e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.0682077, Final residual = 5.46705e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0696703, Final residual = 2.68732e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000257225, Final residual = 2.6643e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0555741, Final residual = 1.51741e-06, No Iterations 4 T gas min/max = 373.921, 433 DICPCG: Solving for p, Initial residual = 0.914379, Final residual = 0.0875726, No Iterations 42 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 8.49907e-05, global = 1.21021e-08, cumulative = 2.1954e-06 DICPCG: Solving for p, Initial residual = 0.555044, Final residual = 9.83546e-07, No Iterations 110 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.27864e-10, global = -3.71823e-15, cumulative = 2.1954e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.269358, Final residual = 3.58348e-06, No Iterations 5 DILUPBiCG: Solving for k, Initial residual = 0.133583, Final residual = 1.86633e-06, No Iterations 5 Mean pressure:100905 Mean temperature:375.32 Mean u':1.04579 ExecutionTime = 665.05 s ClockTime = 674 s Courant Number mean: 0.00265071 max: 0.00565108 deltaT = 0.000656276 Crank angle = -170.656 CA-deg deltaZ = 4.4782e-05 clearance: 0.0996702 Piston speed = 0.0682365 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0922571, Final residual = 9.54251e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.0925664, Final residual = 8.05473e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0673291, Final residual = 2.50614e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000254746, Final residual = 7.6026e-06, No Iterations 3 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0533499, Final residual = 1.42711e-06, No Iterations 4 T gas min/max = 374.014, 433 DICPCG: Solving for p, Initial residual = 0.914953, Final residual = 0.0833109, No Iterations 42 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 8.44547e-05, global = 9.51444e-09, cumulative = 2.20491e-06 DICPCG: Solving for p, Initial residual = 0.568132, Final residual = 9.3891e-07, No Iterations 111 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.27493e-10, global = 4.27072e-14, cumulative = 2.20491e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.275107, Final residual = 3.53192e-06, No Iterations 5 DILUPBiCG: Solving for k, Initial residual = 0.125032, Final residual = 1.67939e-06, No Iterations 5 Mean pressure:100998 Mean temperature:375.501 Mean u':1.0208 ExecutionTime = 679.7 s ClockTime = 688 s Courant Number mean: 0.00259171 max: 0.00582029 deltaT = 0.000656276 Crank angle = -170 CA-deg deltaZ = 4.807e-05 clearance: 0.0996221 Piston speed = 0.0732466 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.088753, Final residual = 4.99307e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.0898099, Final residual = 5.54315e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0630135, Final residual = 2.26407e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000250172, Final residual = 2.59445e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.051476, Final residual = 1.3472e-06, No Iterations 4 T gas min/max = 374.112, 433 DICPCG: Solving for p, Initial residual = 0.917542, Final residual = 0.0745016, No Iterations 43 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 7.84119e-05, global = 6.05129e-09, cumulative = 2.21096e-06 DICPCG: Solving for p, Initial residual = 0.505923, Final residual = 7.56279e-07, No Iterations 113 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.70566e-10, global = 4.07091e-14, cumulative = 2.21096e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.276659, Final residual = 3.42799e-06, No Iterations 5 DILUPBiCG: Solving for k, Initial residual = 0.117523, Final residual = 1.51797e-06, No Iterations 5 Mean pressure:101096 Mean temperature:375.684 Mean u':0.997121 ExecutionTime = 695.99 s ClockTime = 708 s Courant Number mean: 0.00253573 max: 0.00554964 deltaT = 0.000714314 Crank angle = -169.286 CA-deg deltaZ = 5.60651e-05 clearance: 0.0995661 Piston speed = 0.0784879 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0790106, Final residual = 8.49159e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.0773473, Final residual = 8.2841e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0653026, Final residual = 3.06184e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000265345, Final residual = 4.00207e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0541547, Final residual = 1.93034e-06, No Iterations 4 T gas min/max = 374.224, 433 DICPCG: Solving for p, Initial residual = 0.916436, Final residual = 0.0844499, No Iterations 41 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000101023, global = 1.11955e-08, cumulative = 2.22216e-06 DICPCG: Solving for p, Initial residual = 0.552624, Final residual = 9.03476e-07, No Iterations 116 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.3294e-10, global = 3.87998e-14, cumulative = 2.22216e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.281724, Final residual = 4.82962e-06, No Iterations 5 DILUPBiCG: Solving for k, Initial residual = 0.119421, Final residual = 2.14445e-06, No Iterations 5 Mean pressure:101207 Mean temperature:375.887 Mean u':0.972847 ExecutionTime = 710.67 s ClockTime = 723 s Courant Number mean: 0.00269764 max: 0.00611005 deltaT = 0.000857177 Crank angle = -168.429 CA-deg deltaZ = 7.24406e-05 clearance: 0.0994936 Piston speed = 0.0845107 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.12685, Final residual = 2.85024e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.146289, Final residual = 2.46145e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0684654, Final residual = 6.48517e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000305648, Final residual = 1.19114e-06, No Iterations 3 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0626181, Final residual = 4.32479e-06, No Iterations 4 T gas min/max = 374.363, 433 DICPCG: Solving for p, Initial residual = 0.914099, Final residual = 0.0727387, No Iterations 45 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000109752, global = 1.31561e-08, cumulative = 2.23531e-06 DICPCG: Solving for p, Initial residual = 0.521979, Final residual = 8.98227e-07, No Iterations 114 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.00872e-10, global = 1.98337e-14, cumulative = 2.23531e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.296714, Final residual = 1.53427e-06, No Iterations 6 DILUPBiCG: Solving for k, Initial residual = 0.131726, Final residual = 4.86093e-06, No Iterations 5 Mean pressure:101346 Mean temperature:376.133 Mean u':0.945759 ExecutionTime = 725.39 s ClockTime = 738 s Courant Number mean: 0.00315344 max: 0.00767718 deltaT = 0.000857177 Crank angle = -167.571 CA-deg deltaZ = 7.80868e-05 clearance: 0.0994155 Piston speed = 0.0910976 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.200225, Final residual = 3.66744e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.154597, Final residual = 3.38095e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0638458, Final residual = 5.11428e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000310203, Final residual = 9.98839e-07, No Iterations 3 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0605461, Final residual = 4.08583e-06, No Iterations 4 T gas min/max = 374.509, 433 DICPCG: Solving for p, Initial residual = 0.918514, Final residual = 0.0903961, No Iterations 50 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000142261, global = 6.70383e-09, cumulative = 2.24202e-06 DICPCG: Solving for p, Initial residual = 0.585788, Final residual = 9.39311e-07, No Iterations 120 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.47775e-10, global = 1.25808e-14, cumulative = 2.24202e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.292806, Final residual = 9.83015e-06, No Iterations 5 DILUPBiCG: Solving for k, Initial residual = 0.123294, Final residual = 4.37394e-06, No Iterations 5 Mean pressure:101493 Mean temperature:376.384 Mean u':0.920327 ExecutionTime = 740.15 s ClockTime = 753 s Courant Number mean: 0.00307144 max: 0.00774932 deltaT = 0.000857177 Crank angle = -166.714 CA-deg deltaZ = 8.37493e-05 clearance: 0.0993318 Piston speed = 0.0977036 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.122127, Final residual = 2.32003e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.139175, Final residual = 2.604e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0691699, Final residual = 6.15186e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000297825, Final residual = 4.94216e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0589695, Final residual = 3.87825e-06, No Iterations 4 T gas min/max = 374.662, 433 DICPCG: Solving for p, Initial residual = 0.91683, Final residual = 0.0860659, No Iterations 45 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000142236, global = 1.09346e-08, cumulative = 2.25295e-06 DICPCG: Solving for p, Initial residual = 0.54049, Final residual = 9.23162e-07, No Iterations 112 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.47842e-10, global = -8.07634e-15, cumulative = 2.25295e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.286726, Final residual = 9.28975e-06, No Iterations 5 DILUPBiCG: Solving for k, Initial residual = 0.115876, Final residual = 3.95415e-06, No Iterations 5 Mean pressure:101647 Mean temperature:376.639 Mean u':0.896401 ExecutionTime = 754.83 s ClockTime = 767 s Courant Number mean: 0.00299157 max: 0.00740362 deltaT = 0.000857177 Crank angle = -165.857 CA-deg deltaZ = 8.94291e-05 clearance: 0.0992424 Piston speed = 0.10433 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.178638, Final residual = 2.98418e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.161541, Final residual = 2.79003e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0607762, Final residual = 4.47749e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000299687, Final residual = 1.03901e-06, No Iterations 3 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0577042, Final residual = 3.6959e-06, No Iterations 4 T gas min/max = 374.822, 433 DICPCG: Solving for p, Initial residual = 0.916566, Final residual = 0.0824824, No Iterations 50 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000142775, global = 5.41139e-09, cumulative = 2.25836e-06 DICPCG: Solving for p, Initial residual = 0.554433, Final residual = 8.5764e-07, No Iterations 116 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.30245e-10, global = -4.04627e-14, cumulative = 2.25836e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.279717, Final residual = 8.74509e-06, No Iterations 5 DILUPBiCG: Solving for k, Initial residual = 0.109304, Final residual = 3.59238e-06, No Iterations 5 Mean pressure:101808 Mean temperature:376.9 Mean u':0.873844 ExecutionTime = 769.57 s ClockTime = 782 s Courant Number mean: 0.00292184 max: 0.00769821 deltaT = 0.000857177 Crank angle = -165 CA-deg deltaZ = 9.51273e-05 clearance: 0.0991472 Piston speed = 0.110977 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.133092, Final residual = 2.97604e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.135976, Final residual = 3.07363e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0606656, Final residual = 4.8575e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000299282, Final residual = 4.01903e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0566725, Final residual = 3.53032e-06, No Iterations 4 T gas min/max = 374.991, 433 DICPCG: Solving for p, Initial residual = 0.919094, Final residual = 0.0783547, No Iterations 45 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000141413, global = 1.12244e-08, cumulative = 2.26959e-06 DICPCG: Solving for p, Initial residual = 0.517996, Final residual = 8.56097e-07, No Iterations 117 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.28689e-10, global = -2.52733e-14, cumulative = 2.26959e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.272084, Final residual = 8.20747e-06, No Iterations 5 DILUPBiCG: Solving for k, Initial residual = 0.103435, Final residual = 3.28161e-06, No Iterations 5 Mean pressure:101977 Mean temperature:377.167 Mean u':0.852538 ExecutionTime = 786 s ClockTime = 807 s Courant Number mean: 0.00284805 max: 0.00689562 deltaT = 0.00100004 Crank angle = -164 CA-deg deltaZ = 0.00011821 clearance: 0.099029 Piston speed = 0.118205 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.227758, Final residual = 7.59273e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.226042, Final residual = 7.71677e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0640578, Final residual = 7.6016e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000324984, Final residual = 6.88214e-08, No Iterations 5 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0648303, Final residual = 6.85304e-06, No Iterations 4 T gas min/max = 375.196, 433 DICPCG: Solving for p, Initial residual = 0.915605, Final residual = 0.0724386, No Iterations 52 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000160326, global = 1.09145e-08, cumulative = 2.2805e-06 DICPCG: Solving for p, Initial residual = 0.553068, Final residual = 9.36102e-07, No Iterations 122 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.52247e-10, global = -1.06475e-14, cumulative = 2.2805e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.280603, Final residual = 2.38236e-06, No Iterations 6 DILUPBiCG: Solving for k, Initial residual = 0.112161, Final residual = 6.30784e-06, No Iterations 5 Mean pressure:102184 Mean temperature:377.484 Mean u':0.829366 ExecutionTime = 800.8 s ClockTime = 821 s Courant Number mean: 0.00326481 max: 0.0108492 deltaT = 0.00100004 Crank angle = -163 CA-deg deltaZ = 0.000126025 clearance: 0.098903 Piston speed = 0.12602 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.195477, Final residual = 7.97329e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.202136, Final residual = 6.98669e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0542372, Final residual = 7.02152e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000306946, Final residual = 6.90105e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0637501, Final residual = 6.55444e-06, No Iterations 4 T gas min/max = 375.411, 433 DICPCG: Solving for p, Initial residual = 0.922909, Final residual = 0.0909427, No Iterations 47 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000210025, global = 1.58366e-08, cumulative = 2.29634e-06 DICPCG: Solving for p, Initial residual = 0.597344, Final residual = 9.227e-07, No Iterations 125 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.0198e-10, global = 9.74365e-15, cumulative = 2.29634e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.272047, Final residual = 2.2281e-06, No Iterations 6 DILUPBiCG: Solving for k, Initial residual = 0.105901, Final residual = 5.75984e-06, No Iterations 5 Mean pressure:102402 Mean temperature:377.809 Mean u':0.807581 ExecutionTime = 815.49 s ClockTime = 836 s Courant Number mean: 0.00316048 max: 0.00918441 deltaT = 0.00100004 Crank angle = -162 CA-deg deltaZ = 0.000133875 clearance: 0.0987691 Piston speed = 0.13387 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.282684, Final residual = 8.22347e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.279855, Final residual = 7.39533e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0658342, Final residual = 7.23928e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000310025, Final residual = 9.13816e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0630268, Final residual = 6.28382e-06, No Iterations 4 T gas min/max = 375.636, 433 DICPCG: Solving for p, Initial residual = 0.918908, Final residual = 0.0730402, No Iterations 52 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000177898, global = 7.15548e-09, cumulative = 2.30349e-06 DICPCG: Solving for p, Initial residual = 0.59429, Final residual = 8.7207e-07, No Iterations 123 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.976e-10, global = -3.43525e-14, cumulative = 2.30349e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.260874, Final residual = 2.05556e-06, No Iterations 6 DILUPBiCG: Solving for k, Initial residual = 0.100288, Final residual = 5.26568e-06, No Iterations 5 Mean pressure:102630 Mean temperature:378.141 Mean u':0.787062 ExecutionTime = 830.31 s ClockTime = 851 s Courant Number mean: 0.00312323 max: 0.0110911 deltaT = 0.00100004 Crank angle = -161 CA-deg deltaZ = 0.000141762 clearance: 0.0986274 Piston speed = 0.141756 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.197292, Final residual = 7.60309e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.203342, Final residual = 6.7994e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0490299, Final residual = 5.52349e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000302051, Final residual = 4.68634e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0625167, Final residual = 6.04734e-06, No Iterations 4 T gas min/max = 375.873, 433 DICPCG: Solving for p, Initial residual = 0.923058, Final residual = 0.0812707, No Iterations 46 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000206979, global = 1.73775e-08, cumulative = 2.32087e-06 DICPCG: Solving for p, Initial residual = 0.595899, Final residual = 9.53657e-07, No Iterations 121 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.67161e-10, global = -2.21317e-14, cumulative = 2.32087e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.244312, Final residual = 1.85013e-06, No Iterations 6 DILUPBiCG: Solving for k, Initial residual = 0.0952274, Final residual = 4.82782e-06, No Iterations 5 Mean pressure:102869 Mean temperature:378.482 Mean u':0.767698 ExecutionTime = 845.04 s ClockTime = 866 s Courant Number mean: 0.00304187 max: 0.00990427 deltaT = 0.00100004 Crank angle = -160 CA-deg deltaZ = 0.000149687 clearance: 0.0984777 Piston speed = 0.149681 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.297009, Final residual = 8.44339e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.290101, Final residual = 8.65829e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0617298, Final residual = 6.29835e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000293811, Final residual = 4.63014e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0621714, Final residual = 5.84847e-06, No Iterations 4 T gas min/max = 376.12, 433 DICPCG: Solving for p, Initial residual = 0.921874, Final residual = 0.0697322, No Iterations 52 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000186315, global = 1.01879e-08, cumulative = 2.33106e-06 DICPCG: Solving for p, Initial residual = 0.591333, Final residual = 9.19834e-07, No Iterations 123 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.58234e-10, global = -9.83544e-15, cumulative = 2.33106e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.228437, Final residual = 1.66137e-06, No Iterations 6 DILUPBiCG: Solving for k, Initial residual = 0.0906437, Final residual = 4.43817e-06, No Iterations 5 Mean pressure:103120 Mean temperature:378.832 Mean u':0.74939 ExecutionTime = 861.46 s ClockTime = 884 s Courant Number mean: 0.00303891 max: 0.0113527 deltaT = 0.000833367 Crank angle = -159.167 CA-deg deltaZ = 0.000130822 clearance: 0.0983468 Piston speed = 0.15698 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.252056, Final residual = 3.93486e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.18722, Final residual = 3.4219e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0360466, Final residual = 1.92234e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000264098, Final residual = 3.45615e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0518519, Final residual = 2.43137e-06, No Iterations 4 T gas min/max = 376.336, 433 DICPCG: Solving for p, Initial residual = 0.930863, Final residual = 0.0887828, No Iterations 45 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000204291, global = 1.50989e-08, cumulative = 2.34616e-06 DICPCG: Solving for p, Initial residual = 0.60746, Final residual = 9.78472e-07, No Iterations 116 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.29709e-10, global = -6.78011e-15, cumulative = 2.34616e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.190942, Final residual = 4.15985e-06, No Iterations 5 DILUPBiCG: Solving for k, Initial residual = 0.0735704, Final residual = 1.68499e-06, No Iterations 5 Mean pressure:103339 Mean temperature:379.131 Mean u':0.734723 ExecutionTime = 876.19 s ClockTime = 899 s Courant Number mean: 0.00248276 max: 0.00813947 deltaT = 0.000833367 Crank angle = -158.333 CA-deg deltaZ = 0.000136377 clearance: 0.0982105 Piston speed = 0.163646 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.263792, Final residual = 3.63374e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.275816, Final residual = 3.448e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0519271, Final residual = 2.51091e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000266979, Final residual = 1.68122e-07, No Iterations 3 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0519461, Final residual = 2.36682e-06, No Iterations 4 T gas min/max = 376.561, 433 DICPCG: Solving for p, Initial residual = 0.923445, Final residual = 0.0897003, No Iterations 50 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000215158, global = 1.69309e-08, cumulative = 2.36309e-06 DICPCG: Solving for p, Initial residual = 0.642018, Final residual = 8.91713e-07, No Iterations 123 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.90934e-10, global = 3.16338e-14, cumulative = 2.36309e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.180589, Final residual = 3.80705e-06, No Iterations 5 DILUPBiCG: Solving for k, Initial residual = 0.0708237, Final residual = 1.56877e-06, No Iterations 5 Mean pressure:103565 Mean temperature:379.438 Mean u':0.720696 ExecutionTime = 890.98 s ClockTime = 914 s Courant Number mean: 0.00248381 max: 0.00826394 deltaT = 0.000833367 Crank angle = -157.5 CA-deg deltaZ = 0.000141958 clearance: 0.0980685 Piston speed = 0.170342 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.278302, Final residual = 3.69805e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.276326, Final residual = 3.77565e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0340821, Final residual = 1.82764e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000267251, Final residual = 2.29731e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0519735, Final residual = 2.3006e-06, No Iterations 4 T gas min/max = 376.794, 433 DICPCG: Solving for p, Initial residual = 0.92603, Final residual = 0.0892468, No Iterations 47 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000220439, global = 3.6982e-08, cumulative = 2.40007e-06 DICPCG: Solving for p, Initial residual = 0.626499, Final residual = 9.04566e-07, No Iterations 124 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.08967e-10, global = 4.46469e-14, cumulative = 2.40007e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.171849, Final residual = 3.5069e-06, No Iterations 5 DILUPBiCG: Solving for k, Initial residual = 0.068268, Final residual = 1.46472e-06, No Iterations 5 Mean pressure:103800 Mean temperature:379.752 Mean u':0.707268 ExecutionTime = 905.82 s ClockTime = 929 s Courant Number mean: 0.00241416 max: 0.00866333 deltaT = 0.000833367 Crank angle = -156.667 CA-deg deltaZ = 0.000147564 clearance: 0.0979209 Piston speed = 0.17707 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.345677, Final residual = 3.99988e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.34845, Final residual = 3.97836e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0427062, Final residual = 1.84334e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000255494, Final residual = 4.14676e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0520231, Final residual = 2.23616e-06, No Iterations 4 T gas min/max = 377.036, 433 DICPCG: Solving for p, Initial residual = 0.926141, Final residual = 0.0673712, No Iterations 52 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000172474, global = 9.68246e-09, cumulative = 2.40975e-06 DICPCG: Solving for p, Initial residual = 0.612849, Final residual = 9.47439e-07, No Iterations 123 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.22962e-10, global = -9.17498e-15, cumulative = 2.40975e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.163945, Final residual = 3.24037e-06, No Iterations 5 DILUPBiCG: Solving for k, Initial residual = 0.0658809, Final residual = 9.82423e-06, No Iterations 4 Mean pressure:104044 Mean temperature:380.072 Mean u':0.694398 ExecutionTime = 920.62 s ClockTime = 944 s Courant Number mean: 0.00244355 max: 0.00980113 deltaT = 0.000833367 Crank angle = -155.833 CA-deg deltaZ = 0.000153197 clearance: 0.0977677 Piston speed = 0.183829 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.241853, Final residual = 3.04217e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.217193, Final residual = 3.02093e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0350049, Final residual = 1.65223e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000251204, Final residual = 5.77665e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0521151, Final residual = 2.17595e-06, No Iterations 4 T gas min/max = 377.286, 433 DICPCG: Solving for p, Initial residual = 0.931537, Final residual = 0.0852186, No Iterations 45 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000224185, global = 1.86682e-08, cumulative = 2.42842e-06 DICPCG: Solving for p, Initial residual = 0.634746, Final residual = 7.94782e-07, No Iterations 125 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.58842e-10, global = 1.69632e-14, cumulative = 2.42842e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.156742, Final residual = 3.00039e-06, No Iterations 5 DILUPBiCG: Solving for k, Initial residual = 0.0636441, Final residual = 9.23336e-06, No Iterations 4 Mean pressure:104296 Mean temperature:380.399 Mean u':0.682054 ExecutionTime = 935.34 s ClockTime = 958 s Courant Number mean: 0.00239153 max: 0.0106374 deltaT = 0.000833367 Crank angle = -155 CA-deg deltaZ = 0.000158857 clearance: 0.0976089 Piston speed = 0.190621 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.28808, Final residual = 3.26688e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.289154, Final residual = 2.86782e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0387507, Final residual = 1.54071e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000249862, Final residual = 1.91696e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.052252, Final residual = 2.11744e-06, No Iterations 4 T gas min/max = 377.544, 433 DICPCG: Solving for p, Initial residual = 0.930623, Final residual = 0.073315, No Iterations 51 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000199098, global = 5.69149e-09, cumulative = 2.43411e-06 DICPCG: Solving for p, Initial residual = 0.607425, Final residual = 9.35441e-07, No Iterations 116 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.22695e-10, global = -4.43852e-14, cumulative = 2.43411e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.150177, Final residual = 2.78518e-06, No Iterations 5 DILUPBiCG: Solving for k, Initial residual = 0.0615453, Final residual = 8.68195e-06, No Iterations 4 Mean pressure:104557 Mean temperature:380.734 Mean u':0.670204 ExecutionTime = 951.75 s ClockTime = 978 s Courant Number mean: 0.0023954 max: 0.0110326 deltaT = 0.00100004 Crank angle = -154 CA-deg deltaZ = 0.00019814 clearance: 0.0974108 Piston speed = 0.198132 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.276308, Final residual = 8.48781e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.272631, Final residual = 8.2068e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0400788, Final residual = 3.53697e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000279137, Final residual = 4.49998e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0627046, Final residual = 4.89607e-06, No Iterations 4 T gas min/max = 377.864, 433 DICPCG: Solving for p, Initial residual = 0.928475, Final residual = 0.0779941, No Iterations 48 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000263702, global = 2.39913e-08, cumulative = 2.45811e-06 DICPCG: Solving for p, Initial residual = 0.631547, Final residual = 9.82118e-07, No Iterations 120 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 7.1679e-10, global = -5.99344e-14, cumulative = 2.45811e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.163711, Final residual = 6.13165e-06, No Iterations 5 DILUPBiCG: Solving for k, Initial residual = 0.0701863, Final residual = 2.78495e-06, No Iterations 5 Mean pressure:104882 Mean temperature:381.143 Mean u':0.656723 ExecutionTime = 966.52 s ClockTime = 993 s Courant Number mean: 0.00280453 max: 0.0123408 deltaT = 0.00100004 Crank angle = -153 CA-deg deltaZ = 0.000206381 clearance: 0.0972044 Piston speed = 0.206372 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.380573, Final residual = 9.20936e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.379462, Final residual = 8.7834e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0376751, Final residual = 2.75653e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.00025987, Final residual = 6.79915e-06, No Iterations 3 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0628416, Final residual = 4.75553e-06, No Iterations 4 T gas min/max = 378.195, 433 DICPCG: Solving for p, Initial residual = 0.931408, Final residual = 0.0599873, No Iterations 53 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000209914, global = 8.94293e-09, cumulative = 2.46705e-06 DICPCG: Solving for p, Initial residual = 0.622023, Final residual = 9.77772e-07, No Iterations 121 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 7.48964e-10, global = -6.94283e-14, cumulative = 2.46705e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.157125, Final residual = 5.69909e-06, No Iterations 5 DILUPBiCG: Solving for k, Initial residual = 0.0675855, Final residual = 2.59718e-06, No Iterations 5 Mean pressure:105220 Mean temperature:381.561 Mean u':0.643856 ExecutionTime = 981.3 s ClockTime = 1008 s Courant Number mean: 0.00285408 max: 0.0143484 deltaT = 0.00100004 Crank angle = -152 CA-deg deltaZ = 0.000214673 clearance: 0.0969897 Piston speed = 0.214664 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.306332, Final residual = 9.5022e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.309403, Final residual = 8.92462e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0439136, Final residual = 3.59468e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000257459, Final residual = 5.67335e-07, No Iterations 3 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.063193, Final residual = 4.63935e-06, No Iterations 4 T gas min/max = 378.538, 433 DICPCG: Solving for p, Initial residual = 0.934297, Final residual = 0.0913603, No Iterations 46 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000332441, global = 3.23438e-08, cumulative = 2.49939e-06 DICPCG: Solving for p, Initial residual = 0.681195, Final residual = 9.99947e-07, No Iterations 114 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 8.75184e-10, global = 3.12448e-14, cumulative = 2.49939e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.150615, Final residual = 5.29231e-06, No Iterations 5 DILUPBiCG: Solving for k, Initial residual = 0.0651564, Final residual = 2.42526e-06, No Iterations 5 Mean pressure:105571 Mean temperature:381.99 Mean u':0.631562 ExecutionTime = 996.02 s ClockTime = 1023 s Courant Number mean: 0.0028154 max: 0.0153793 deltaT = 0.00100004 Crank angle = -151 CA-deg deltaZ = 0.000223017 clearance: 0.0967667 Piston speed = 0.223008 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.422693, Final residual = 9.38135e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.429204, Final residual = 8.94365e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0358572, Final residual = 2.32491e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.00025951, Final residual = 1.67113e-06, No Iterations 3 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.063651, Final residual = 4.53101e-06, No Iterations 4 T gas min/max = 378.895, 433 DICPCG: Solving for p, Initial residual = 0.931534, Final residual = 0.0907978, No Iterations 52 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000344268, global = 1.61706e-08, cumulative = 2.51556e-06 DICPCG: Solving for p, Initial residual = 0.701336, Final residual = 9.52172e-07, No Iterations 118 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 8.83929e-10, global = -7.37312e-14, cumulative = 2.51556e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.14459, Final residual = 4.92502e-06, No Iterations 5 DILUPBiCG: Solving for k, Initial residual = 0.0628785, Final residual = 2.26882e-06, No Iterations 5 Mean pressure:105935 Mean temperature:382.43 Mean u':0.619804 ExecutionTime = 1010.82 s ClockTime = 1038 s Courant Number mean: 0.00291582 max: 0.0184243 deltaT = 0.00050002 Crank angle = -150.5 CA-deg deltaZ = 0.000114654 clearance: 0.096652 Piston speed = 0.2293 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.195084, Final residual = 2.50831e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.197743, Final residual = 2.10547e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0221294, Final residual = 1.68419e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000175373, Final residual = 5.86444e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0323823, Final residual = 2.14218e-06, No Iterations 3 T gas min/max = 379.079, 433 DICPCG: Solving for p, Initial residual = 0.94749, Final residual = 0.0881414, No Iterations 41 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000166617, global = 2.15745e-08, cumulative = 2.53714e-06 DICPCG: Solving for p, Initial residual = 0.619825, Final residual = 9.72514e-07, No Iterations 106 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.79657e-10, global = -1.056e-13, cumulative = 2.53714e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0808069, Final residual = 1.40978e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0319574, Final residual = 6.76046e-06, No Iterations 3 Mean pressure:106123 Mean temperature:382.656 Mean u':0.61396 ExecutionTime = 1025.39 s ClockTime = 1052 s Courant Number mean: 0.00144619 max: 0.00954432 deltaT = 0.00050002 Crank angle = -150 CA-deg deltaZ = 0.000116761 clearance: 0.0965353 Piston speed = 0.233512 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.172283, Final residual = 1.99267e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.176389, Final residual = 2.00987e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0283824, Final residual = 1.91349e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.00018126, Final residual = 4.29881e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0328254, Final residual = 2.14011e-06, No Iterations 3 T gas min/max = 379.269, 433 DICPCG: Solving for p, Initial residual = 0.93421, Final residual = 0.0617979, No Iterations 41 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000119983, global = 1.68507e-08, cumulative = 2.55399e-06 DICPCG: Solving for p, Initial residual = 0.566499, Final residual = 8.38226e-07, No Iterations 105 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.63286e-10, global = -4.72314e-14, cumulative = 2.55399e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0787588, Final residual = 1.34544e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0314136, Final residual = 6.52182e-06, No Iterations 3 Mean pressure:106316 Mean temperature:382.887 Mean u':0.608244 ExecutionTime = 1041.59 s ClockTime = 1070 s Courant Number mean: 0.00144848 max: 0.00940828 deltaT = 0.000555578 Crank angle = -149.444 CA-deg deltaZ = 0.000132213 clearance: 0.0964031 Piston speed = 0.237974 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.131731, Final residual = 2.28527e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.132991, Final residual = 1.89709e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0175784, Final residual = 1.62077e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000191387, Final residual = 9.9798e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0366937, Final residual = 3.40379e-06, No Iterations 3 T gas min/max = 379.485, 433 DICPCG: Solving for p, Initial residual = 0.938934, Final residual = 0.0739216, No Iterations 41 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000161165, global = 2.32958e-08, cumulative = 2.57728e-06 DICPCG: Solving for p, Initial residual = 0.609197, Final residual = 8.22235e-07, No Iterations 113 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.91721e-10, global = 4.74737e-14, cumulative = 2.57728e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0842228, Final residual = 2.15728e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0341281, Final residual = 9.6472e-06, No Iterations 3 Mean pressure:106533 Mean temperature:383.147 Mean u':0.602054 ExecutionTime = 1056.19 s ClockTime = 1085 s Courant Number mean: 0.00159231 max: 0.0102904 deltaT = 0.000634946 Crank angle = -148.81 CA-deg deltaZ = 0.000154307 clearance: 0.0962487 Piston speed = 0.243024 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.17095, Final residual = 4.20797e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.173019, Final residual = 4.58169e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0221666, Final residual = 3.16935e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000203733, Final residual = 8.12267e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0420834, Final residual = 6.03991e-06, No Iterations 3 T gas min/max = 379.736, 433 DICPCG: Solving for p, Initial residual = 0.938527, Final residual = 0.0816989, No Iterations 41 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000207545, global = 2.93617e-08, cumulative = 2.60665e-06 DICPCG: Solving for p, Initial residual = 0.646571, Final residual = 8.19483e-07, No Iterations 113 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.54358e-10, global = -1.13318e-14, cumulative = 2.60665e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0919432, Final residual = 3.87313e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0379884, Final residual = 1.60043e-06, No Iterations 4 Mean pressure:106788 Mean temperature:383.449 Mean u':0.595185 ExecutionTime = 1070.82 s ClockTime = 1100 s Courant Number mean: 0.00181984 max: 0.0120013 deltaT = 0.000761935 Crank angle = -148.048 CA-deg deltaZ = 0.000189703 clearance: 0.096059 Piston speed = 0.248975 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.22429, Final residual = 1.08546e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.226874, Final residual = 8.17033e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0244808, Final residual = 6.78598e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000221129, Final residual = 1.20147e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0506327, Final residual = 1.11196e-06, No Iterations 4 T gas min/max = 380.044, 433 DICPCG: Solving for p, Initial residual = 0.93736, Final residual = 0.0828443, No Iterations 44 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000258314, global = 3.58623e-08, cumulative = 2.64251e-06 DICPCG: Solving for p, Initial residual = 0.628722, Final residual = 7.65042e-07, No Iterations 118 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.05152e-10, global = -1.03902e-14, cumulative = 2.64251e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.103844, Final residual = 8.36692e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0440972, Final residual = 3.59792e-06, No Iterations 4 Mean pressure:107101 Mean temperature:383.815 Mean u':0.587233 ExecutionTime = 1085.48 s ClockTime = 1114 s Courant Number mean: 0.0021369 max: 0.0128999 deltaT = 0.000761935 Crank angle = -147.286 CA-deg deltaZ = 0.000194674 clearance: 0.0958644 Piston speed = 0.255499 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.338134, Final residual = 1.44887e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.331013, Final residual = 1.3616e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0254172, Final residual = 6.14875e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000215951, Final residual = 3.46998e-06, No Iterations 3 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0508989, Final residual = 1.08522e-06, No Iterations 4 T gas min/max = 380.358, 433 DICPCG: Solving for p, Initial residual = 0.940011, Final residual = 0.0855116, No Iterations 50 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000272426, global = 1.5295e-08, cumulative = 2.6578e-06 DICPCG: Solving for p, Initial residual = 0.644431, Final residual = 9.97776e-07, No Iterations 117 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.61399e-10, global = 2.17781e-15, cumulative = 2.6578e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.101217, Final residual = 7.97115e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0430303, Final residual = 3.42602e-06, No Iterations 4 Mean pressure:107422 Mean temperature:384.188 Mean u':0.579528 ExecutionTime = 1100.27 s ClockTime = 1129 s Courant Number mean: 0.00219165 max: 0.0140338 deltaT = 0.000761935 Crank angle = -146.524 CA-deg deltaZ = 0.000199669 clearance: 0.0956647 Piston speed = 0.262055 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.230792, Final residual = 1.14924e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.230507, Final residual = 1.03697e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0268409, Final residual = 7.13914e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000214031, Final residual = 1.79061e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0512907, Final residual = 1.06343e-06, No Iterations 4 T gas min/max = 380.68, 433 DICPCG: Solving for p, Initial residual = 0.94029, Final residual = 0.0768421, No Iterations 44 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000250568, global = 2.57049e-08, cumulative = 2.68351e-06 DICPCG: Solving for p, Initial residual = 0.598501, Final residual = 8.79921e-07, No Iterations 117 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.74159e-10, global = -1.32946e-14, cumulative = 2.68351e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0985919, Final residual = 7.587e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0420071, Final residual = 3.26459e-06, No Iterations 4 Mean pressure:107752 Mean temperature:384.568 Mean u':0.572057 ExecutionTime = 1114.95 s ClockTime = 1144 s Courant Number mean: 0.00215686 max: 0.0153513 deltaT = 0.000761935 Crank angle = -145.762 CA-deg deltaZ = 0.000204691 clearance: 0.09546 Piston speed = 0.268646 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.292378, Final residual = 1.02528e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.290395, Final residual = 7.33609e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0250972, Final residual = 5.6533e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000206663, Final residual = 5.91318e-07, No Iterations 3 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.051735, Final residual = 1.04316e-06, No Iterations 4 T gas min/max = 381.01, 433 DICPCG: Solving for p, Initial residual = 0.940351, Final residual = 0.086589, No Iterations 49 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00028906, global = 8.86167e-09, cumulative = 2.69237e-06 DICPCG: Solving for p, Initial residual = 0.626819, Final residual = 9.3373e-07, No Iterations 111 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.31878e-10, global = 2.9555e-14, cumulative = 2.69237e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0960945, Final residual = 7.22676e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0410243, Final residual = 3.11259e-06, No Iterations 4 Mean pressure:108092 Mean temperature:384.954 Mean u':0.564812 ExecutionTime = 1129.64 s ClockTime = 1159 s Courant Number mean: 0.00219157 max: 0.0149221 deltaT = 0.000761935 Crank angle = -145 CA-deg deltaZ = 0.000209738 clearance: 0.0952503 Piston speed = 0.27527 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.213679, Final residual = 8.47638e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.208568, Final residual = 8.85755e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0253372, Final residual = 6.44168e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000212534, Final residual = 6.10718e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0522104, Final residual = 1.02412e-06, No Iterations 4 T gas min/max = 381.349, 433 DICPCG: Solving for p, Initial residual = 0.940886, Final residual = 0.0783815, No Iterations 44 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000267797, global = 2.44724e-08, cumulative = 2.71684e-06 DICPCG: Solving for p, Initial residual = 0.600185, Final residual = 7.87912e-07, No Iterations 117 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.40424e-10, global = -4.21673e-14, cumulative = 2.71684e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0937173, Final residual = 6.88862e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.040081, Final residual = 2.96886e-06, No Iterations 4 Mean pressure:108440 Mean temperature:385.348 Mean u':0.557783 ExecutionTime = 1145.91 s ClockTime = 1178 s Courant Number mean: 0.00213541 max: 0.0151113 deltaT = 0.000833367 Crank angle = -144.167 CA-deg deltaZ = 0.00023521 clearance: 0.0950151 Piston speed = 0.282241 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.29973, Final residual = 1.46046e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.29713, Final residual = 1.34681e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0267065, Final residual = 7.87895e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000217647, Final residual = 1.28468e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0575947, Final residual = 1.58761e-06, No Iterations 4 T gas min/max = 381.728, 433 DICPCG: Solving for p, Initial residual = 0.938608, Final residual = 0.0868351, No Iterations 50 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000333192, global = 8.89169e-09, cumulative = 2.72573e-06 DICPCG: Solving for p, Initial residual = 0.642238, Final residual = 9.1083e-07, No Iterations 118 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.99945e-10, global = 2.36305e-14, cumulative = 2.72573e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0981145, Final residual = 9.68447e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0425675, Final residual = 4.2566e-06, No Iterations 4 Mean pressure:108832 Mean temperature:385.787 Mean u':0.550355 ExecutionTime = 1160.65 s ClockTime = 1192 s Courant Number mean: 0.00237981 max: 0.015833 deltaT = 0.000833367 Crank angle = -143.333 CA-deg deltaZ = 0.000241314 clearance: 0.0947737 Piston speed = 0.289565 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.226624, Final residual = 1.35096e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.234951, Final residual = 1.47905e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0247048, Final residual = 7.74071e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000217145, Final residual = 4.33735e-07, No Iterations 3 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0581525, Final residual = 1.55761e-06, No Iterations 4 T gas min/max = 382.117, 433 DICPCG: Solving for p, Initial residual = 0.940526, Final residual = 0.0790102, No Iterations 45 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000310203, global = 2.25955e-08, cumulative = 2.74833e-06 DICPCG: Solving for p, Initial residual = 0.604973, Final residual = 9.81205e-07, No Iterations 126 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 6.46211e-10, global = 8.03469e-14, cumulative = 2.74833e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0956931, Final residual = 9.23323e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0415325, Final residual = 4.05301e-06, No Iterations 4 Mean pressure:109236 Mean temperature:386.235 Mean u':0.543162 ExecutionTime = 1175.44 s ClockTime = 1207 s Courant Number mean: 0.00232558 max: 0.0163279 deltaT = 0.000833367 Crank angle = -142.5 CA-deg deltaZ = 0.000247451 clearance: 0.0945263 Piston speed = 0.296929 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.292963, Final residual = 1.52208e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.300592, Final residual = 1.31377e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0271589, Final residual = 7.73617e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000211719, Final residual = 2.61163e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0587943, Final residual = 1.53145e-06, No Iterations 4 T gas min/max = 382.517, 433 DICPCG: Solving for p, Initial residual = 0.941466, Final residual = 0.0902234, No Iterations 50 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000362823, global = 9.15514e-09, cumulative = 2.75748e-06 DICPCG: Solving for p, Initial residual = 0.649801, Final residual = 6.88204e-07, No Iterations 111 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.81102e-10, global = -2.15956e-14, cumulative = 2.75748e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0933134, Final residual = 8.80166e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0405386, Final residual = 3.86292e-06, No Iterations 4 Mean pressure:109651 Mean temperature:386.691 Mean u':0.536193 ExecutionTime = 1190.13 s ClockTime = 1222 s Courant Number mean: 0.00236663 max: 0.0140982 deltaT = 0.000833367 Crank angle = -141.667 CA-deg deltaZ = 0.000253623 clearance: 0.0942727 Piston speed = 0.304335 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.263774, Final residual = 1.42044e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.242906, Final residual = 1.40616e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0236037, Final residual = 6.95997e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000213278, Final residual = 1.94866e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0594805, Final residual = 1.50737e-06, No Iterations 4 T gas min/max = 382.927, 433 DICPCG: Solving for p, Initial residual = 0.940572, Final residual = 0.0888424, No Iterations 45 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000366577, global = 2.93145e-08, cumulative = 2.7868e-06 DICPCG: Solving for p, Initial residual = 0.645034, Final residual = 8.85626e-07, No Iterations 117 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 6.49268e-10, global = 3.014e-14, cumulative = 2.7868e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0910523, Final residual = 8.40016e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0395826, Final residual = 3.68451e-06, No Iterations 4 Mean pressure:110078 Mean temperature:387.157 Mean u':0.529437 ExecutionTime = 1204.81 s ClockTime = 1237 s Courant Number mean: 0.00232557 max: 0.0164353 deltaT = 0.000833367 Crank angle = -140.833 CA-deg deltaZ = 0.000259829 clearance: 0.0940128 Piston speed = 0.311783 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.339005, Final residual = 1.65e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.333268, Final residual = 1.74402e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0274404, Final residual = 7.67553e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000211073, Final residual = 1.76985e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0602006, Final residual = 1.48515e-06, No Iterations 4 T gas min/max = 383.347, 433 DICPCG: Solving for p, Initial residual = 0.940108, Final residual = 0.087328, No Iterations 50 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000369453, global = 9.42559e-09, cumulative = 2.79622e-06 DICPCG: Solving for p, Initial residual = 0.64991, Final residual = 9.69908e-07, No Iterations 120 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 7.10261e-10, global = 5.50209e-14, cumulative = 2.79622e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0888848, Final residual = 8.01745e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0386639, Final residual = 3.51478e-06, No Iterations 4 Mean pressure:110518 Mean temperature:387.633 Mean u':0.522887 ExecutionTime = 1219.57 s ClockTime = 1251 s Courant Number mean: 0.00237014 max: 0.0151961 deltaT = 0.000833367 Crank angle = -140 CA-deg deltaZ = 0.00026607 clearance: 0.0937468 Piston speed = 0.319272 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.24944, Final residual = 1.13621e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.258901, Final residual = 1.3249e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0218401, Final residual = 6.11031e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000205349, Final residual = 4.29078e-07, No Iterations 3 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0609529, Final residual = 1.46334e-06, No Iterations 4 T gas min/max = 383.779, 433 DICPCG: Solving for p, Initial residual = 0.941386, Final residual = 0.0800692, No Iterations 45 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000346591, global = 2.68408e-08, cumulative = 2.82307e-06 DICPCG: Solving for p, Initial residual = 0.621183, Final residual = 9.28997e-07, No Iterations 127 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 6.75917e-10, global = -1.09393e-13, cumulative = 2.82306e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0868261, Final residual = 7.6645e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0377778, Final residual = 3.35653e-06, No Iterations 4 Mean pressure:110970 Mean temperature:388.118 Mean u':0.516532 ExecutionTime = 1236.01 s ClockTime = 1270 s Courant Number mean: 0.00233534 max: 0.0159908 deltaT = 0.000833367 Crank angle = -139.167 CA-deg deltaZ = 0.000272346 clearance: 0.0934744 Piston speed = 0.326802 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.326044, Final residual = 1.52178e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.321009, Final residual = 1.40803e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0275494, Final residual = 7.39052e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000208455, Final residual = 2.17393e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0617372, Final residual = 1.44394e-06, No Iterations 4 T gas min/max = 384.222, 433 DICPCG: Solving for p, Initial residual = 0.941945, Final residual = 0.0867321, No Iterations 50 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000384327, global = 1.07014e-08, cumulative = 2.83377e-06 DICPCG: Solving for p, Initial residual = 0.650846, Final residual = 8.39102e-07, No Iterations 118 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 6.30174e-10, global = 1.88443e-13, cumulative = 2.83377e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.084844, Final residual = 7.33048e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0369256, Final residual = 3.20751e-06, No Iterations 4 Mean pressure:111435 Mean temperature:388.613 Mean u':0.510365 ExecutionTime = 1250.75 s ClockTime = 1285 s Courant Number mean: 0.00240758 max: 0.0139043 deltaT = 0.000833367 Crank angle = -138.333 CA-deg deltaZ = 0.000278655 clearance: 0.0931958 Piston speed = 0.334373 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.254545, Final residual = 1.29987e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.245518, Final residual = 1.22294e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0196791, Final residual = 5.15322e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000208603, Final residual = 8.24528e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0625525, Final residual = 1.42562e-06, No Iterations 4 T gas min/max = 384.676, 433 DICPCG: Solving for p, Initial residual = 0.942402, Final residual = 0.0917894, No Iterations 44 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000416319, global = 3.48792e-08, cumulative = 2.86865e-06 DICPCG: Solving for p, Initial residual = 0.659553, Final residual = 8.5511e-07, No Iterations 118 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 6.88654e-10, global = -1.93737e-13, cumulative = 2.86865e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0829636, Final residual = 7.02042e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0361003, Final residual = 3.06726e-06, No Iterations 4 Mean pressure:111913 Mean temperature:389.119 Mean u':0.504378 ExecutionTime = 1265.42 s ClockTime = 1300 s Courant Number mean: 0.0023628 max: 0.0156695 deltaT = 0.000833367 Crank angle = -137.5 CA-deg deltaZ = 0.000284999 clearance: 0.0929108 Piston speed = 0.341985 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.347097, Final residual = 1.79665e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.366085, Final residual = 1.9067e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0296881, Final residual = 7.88821e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000206804, Final residual = 6.01908e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0633999, Final residual = 1.4089e-06, No Iterations 4 T gas min/max = 385.141, 433 DICPCG: Solving for p, Initial residual = 0.940557, Final residual = 0.0855639, No Iterations 50 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00039811, global = 1.79079e-08, cumulative = 2.88655e-06 DICPCG: Solving for p, Initial residual = 0.664102, Final residual = 9.21115e-07, No Iterations 121 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 7.35095e-10, global = 8.83642e-14, cumulative = 2.88655e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0811414, Final residual = 6.72342e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0353075, Final residual = 2.93429e-06, No Iterations 4 Mean pressure:112405 Mean temperature:389.634 Mean u':0.498563 ExecutionTime = 1280.14 s ClockTime = 1314 s Courant Number mean: 0.00245102 max: 0.0161006 deltaT = 0.000833367 Crank angle = -136.667 CA-deg deltaZ = 0.000291377 clearance: 0.0926194 Piston speed = 0.349638 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.283746, Final residual = 1.29983e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.299893, Final residual = 1.34944e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0163955, Final residual = 3.95861e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000204904, Final residual = 1.10805e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0642788, Final residual = 1.39246e-06, No Iterations 4 T gas min/max = 385.618, 433 DICPCG: Solving for p, Initial residual = 0.942565, Final residual = 0.0904418, No Iterations 44 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000429819, global = 4.1486e-08, cumulative = 2.92804e-06 DICPCG: Solving for p, Initial residual = 0.664078, Final residual = 8.30236e-07, No Iterations 127 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 6.99843e-10, global = -6.08557e-14, cumulative = 2.92804e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0794186, Final residual = 6.44874e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0345353, Final residual = 2.80884e-06, No Iterations 4 Mean pressure:112911 Mean temperature:390.161 Mean u':0.492916 ExecutionTime = 1294.93 s ClockTime = 1329 s Courant Number mean: 0.00239119 max: 0.0140378 deltaT = 0.000833367 Crank angle = -135.833 CA-deg deltaZ = 0.000297788 clearance: 0.0923216 Piston speed = 0.357331 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.402057, Final residual = 1.57097e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.365668, Final residual = 1.36719e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0325791, Final residual = 8.41285e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000207038, Final residual = 4.80681e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0651901, Final residual = 1.3777e-06, No Iterations 4 T gas min/max = 386.107, 433 DICPCG: Solving for p, Initial residual = 0.940739, Final residual = 0.0712128, No Iterations 51 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000347016, global = 2.32934e-08, cumulative = 2.95133e-06 DICPCG: Solving for p, Initial residual = 0.617729, Final residual = 8.51613e-07, No Iterations 124 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 6.63676e-10, global = -4.76637e-14, cumulative = 2.95133e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0777307, Final residual = 6.18679e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0337955, Final residual = 2.69187e-06, No Iterations 4 Mean pressure:113431 Mean temperature:390.698 Mean u':0.487426 ExecutionTime = 1309.67 s ClockTime = 1344 s Courant Number mean: 0.00251714 max: 0.0150317 deltaT = 0.000833367 Crank angle = -135 CA-deg deltaZ = 0.000304232 clearance: 0.0920174 Piston speed = 0.365063 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.275332, Final residual = 1.36211e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.276546, Final residual = 9.44623e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0137291, Final residual = 2.69963e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000205828, Final residual = 4.13951e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0661344, Final residual = 1.36407e-06, No Iterations 4 T gas min/max = 386.608, 433 DICPCG: Solving for p, Initial residual = 0.945554, Final residual = 0.0940976, No Iterations 44 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000466778, global = 4.71289e-08, cumulative = 2.99846e-06 DICPCG: Solving for p, Initial residual = 0.673063, Final residual = 8.58525e-07, No Iterations 116 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 7.54208e-10, global = -1.44598e-13, cumulative = 2.99846e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0761472, Final residual = 5.94341e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0330698, Final residual = 2.57947e-06, No Iterations 4 Mean pressure:113965 Mean temperature:391.246 Mean u':0.482091 ExecutionTime = 1326.07 s ClockTime = 1364 s Courant Number mean: 0.00246395 max: 0.0164183 deltaT = 0.00100004 Crank angle = -134 CA-deg deltaZ = 0.00037363 clearance: 0.0916437 Piston speed = 0.373615 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.427056, Final residual = 4.25653e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.454949, Final residual = 4.24804e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0438521, Final residual = 1.93765e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000231388, Final residual = 1.52494e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0803899, Final residual = 3.36693e-06, No Iterations 4 T gas min/max = 387.224, 433 DICPCG: Solving for p, Initial residual = 0.936696, Final residual = 0.0898858, No Iterations 53 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000553017, global = 4.74734e-08, cumulative = 3.04593e-06 DICPCG: Solving for p, Initial residual = 0.69122, Final residual = 9.8191e-07, No Iterations 127 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.10103e-09, global = -1.66431e-13, cumulative = 3.04593e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0861654, Final residual = 1.75567e-06, No Iterations 5 DILUPBiCG: Solving for k, Initial residual = 0.0383467, Final residual = 5.57908e-06, No Iterations 4 Mean pressure:114626 Mean temperature:391.916 Mean u':0.475923 ExecutionTime = 1340.9 s ClockTime = 1379 s Courant Number mean: 0.00316934 max: 0.0199791 deltaT = 0.00100004 Crank angle = -133 CA-deg deltaZ = 0.000383011 clearance: 0.0912607 Piston speed = 0.382996 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.403365, Final residual = 2.97294e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.41886, Final residual = 3.53881e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0141556, Final residual = 4.87131e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000229903, Final residual = 3.61746e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0816314, Final residual = 3.33134e-06, No Iterations 4 T gas min/max = 387.855, 433 DICPCG: Solving for p, Initial residual = 0.942443, Final residual = 0.0870067, No Iterations 53 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000546642, global = 4.63452e-08, cumulative = 3.09228e-06 DICPCG: Solving for p, Initial residual = 0.685886, Final residual = 9.14964e-07, No Iterations 126 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.06382e-09, global = -2.0816e-14, cumulative = 3.09228e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0843206, Final residual = 1.67751e-06, No Iterations 5 DILUPBiCG: Solving for k, Initial residual = 0.0373819, Final residual = 5.32245e-06, No Iterations 4 Mean pressure:115308 Mean temperature:392.601 Mean u':0.469958 ExecutionTime = 1355.78 s ClockTime = 1394 s Courant Number mean: 0.00324449 max: 0.0221829 deltaT = 0.00100004 Crank angle = -132 CA-deg deltaZ = 0.000392446 clearance: 0.0908683 Piston speed = 0.392431 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.376744, Final residual = 3.9646e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.402398, Final residual = 3.92354e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0393631, Final residual = 1.694e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000230094, Final residual = 4.94246e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0830955, Final residual = 3.31012e-06, No Iterations 4 T gas min/max = 388.505, 433 DICPCG: Solving for p, Initial residual = 0.941791, Final residual = 0.0786868, No Iterations 55 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000507755, global = 2.03071e-08, cumulative = 3.11259e-06 DICPCG: Solving for p, Initial residual = 0.647259, Final residual = 8.83218e-07, No Iterations 128 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 9.85947e-10, global = -3.81143e-14, cumulative = 3.11259e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0823697, Final residual = 1.60116e-06, No Iterations 5 DILUPBiCG: Solving for k, Initial residual = 0.0364636, Final residual = 5.08405e-06, No Iterations 4 Mean pressure:116013 Mean temperature:393.302 Mean u':0.464184 ExecutionTime = 1370.68 s ClockTime = 1409 s Courant Number mean: 0.00344538 max: 0.0229993 deltaT = 0.00100004 Crank angle = -131 CA-deg deltaZ = 0.000401934 clearance: 0.0904664 Piston speed = 0.401918 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.299459, Final residual = 2.73391e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.309706, Final residual = 2.64572e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0159841, Final residual = 5.78575e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000227288, Final residual = 1.4279e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0846663, Final residual = 3.29221e-06, No Iterations 4 T gas min/max = 389.173, 433 DICPCG: Solving for p, Initial residual = 0.943248, Final residual = 0.0933352, No Iterations 47 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000617434, global = 9.08915e-08, cumulative = 3.20348e-06 DICPCG: Solving for p, Initial residual = 0.692876, Final residual = 9.61524e-07, No Iterations 124 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.17573e-09, global = -4.56714e-14, cumulative = 3.20348e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0805502, Final residual = 1.5309e-06, No Iterations 5 DILUPBiCG: Solving for k, Initial residual = 0.0355618, Final residual = 4.85471e-06, No Iterations 4 Mean pressure:116741 Mean temperature:394.021 Mean u':0.458597 ExecutionTime = 1385.41 s ClockTime = 1423 s Courant Number mean: 0.00344289 max: 0.0232459 deltaT = 0.00050002 Crank angle = -130.5 CA-deg deltaZ = 0.00020454 clearance: 0.0902618 Piston speed = 0.409064 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.272242, Final residual = 9.75503e-07, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.270688, Final residual = 9.64438e-06, No Iterations 3 DILUPBiCG: Solving for Uz, Initial residual = 0.0222286, Final residual = 1.11383e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000161091, Final residual = 3.10787e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0433532, Final residual = 1.77174e-06, No Iterations 3 T gas min/max = 389.517, 433 DICPCG: Solving for p, Initial residual = 0.957821, Final residual = 0.0796406, No Iterations 41 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000265604, global = 4.70766e-08, cumulative = 3.25056e-06 DICPCG: Solving for p, Initial residual = 0.618167, Final residual = 9.79962e-07, No Iterations 113 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.04759e-10, global = -3.63414e-14, cumulative = 3.25056e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0439776, Final residual = 5.90976e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0180242, Final residual = 2.49489e-06, No Iterations 3 Mean pressure:117115 Mean temperature:394.39 Mean u':0.455815 ExecutionTime = 1399.99 s ClockTime = 1438 s Courant Number mean: 0.00172228 max: 0.0112038 deltaT = 0.00050002 Crank angle = -130 CA-deg deltaZ = 0.000206931 clearance: 0.0900549 Piston speed = 0.413845 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.224486, Final residual = 9.5196e-06, No Iterations 3 DILUPBiCG: Solving for Uy, Initial residual = 0.215036, Final residual = 8.60865e-06, No Iterations 3 DILUPBiCG: Solving for Uz, Initial residual = 0.0155282, Final residual = 5.35078e-07, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000168367, Final residual = 3.51941e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0441323, Final residual = 1.78374e-06, No Iterations 3 T gas min/max = 389.869, 433 DICPCG: Solving for p, Initial residual = 0.947369, Final residual = 0.0886122, No Iterations 40 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000303436, global = 5.17444e-08, cumulative = 3.3023e-06 DICPCG: Solving for p, Initial residual = 0.677956, Final residual = 8.91285e-07, No Iterations 114 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.67156e-10, global = 2.44385e-14, cumulative = 3.3023e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.043357, Final residual = 5.76851e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0178056, Final residual = 2.43629e-06, No Iterations 3 Mean pressure:117496 Mean temperature:394.766 Mean u':0.453078 ExecutionTime = 1416.22 s ClockTime = 1457 s Courant Number mean: 0.00176005 max: 0.0113106 deltaT = 0.000555578 Crank angle = -129.444 CA-deg deltaZ = 0.000232734 clearance: 0.0898222 Piston speed = 0.418905 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.20372, Final residual = 1.1725e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.205218, Final residual = 1.20629e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0125257, Final residual = 8.20591e-07, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000173763, Final residual = 8.75338e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0496064, Final residual = 2.88538e-06, No Iterations 3 T gas min/max = 390.267, 433 DICPCG: Solving for p, Initial residual = 0.947687, Final residual = 0.0767173, No Iterations 41 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000295883, global = 5.24712e-08, cumulative = 3.35477e-06 DICPCG: Solving for p, Initial residual = 0.653358, Final residual = 9.35886e-07, No Iterations 115 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.1475e-10, global = 1.90101e-14, cumulative = 3.35477e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0469922, Final residual = 8.68559e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0194623, Final residual = 3.69601e-06, No Iterations 3 Mean pressure:117927 Mean temperature:395.19 Mean u':0.450094 ExecutionTime = 1430.82 s ClockTime = 1471 s Courant Number mean: 0.00193491 max: 0.0116991 deltaT = 0.000634946 Crank angle = -128.81 CA-deg deltaZ = 0.000269615 clearance: 0.0895525 Piston speed = 0.424627 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.277532, Final residual = 2.47887e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.265572, Final residual = 2.29797e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.016151, Final residual = 1.45324e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000178059, Final residual = 1.19308e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0572651, Final residual = 5.21516e-06, No Iterations 3 T gas min/max = 390.728, 433 DICPCG: Solving for p, Initial residual = 0.947938, Final residual = 0.090527, No Iterations 42 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000404801, global = 9.97182e-08, cumulative = 3.45449e-06 DICPCG: Solving for p, Initial residual = 0.701418, Final residual = 8.52337e-07, No Iterations 125 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.9861e-10, global = -2.42863e-14, cumulative = 3.45449e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.05208, Final residual = 1.25866e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0218149, Final residual = 6.20026e-06, No Iterations 3 Mean pressure:118429 Mean temperature:395.681 Mean u':0.446758 ExecutionTime = 1445.5 s ClockTime = 1486 s Courant Number mean: 0.00231074 max: 0.013905 deltaT = 0.000761935 Crank angle = -128.048 CA-deg deltaZ = 0.000328669 clearance: 0.0892239 Piston speed = 0.431361 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.368145, Final residual = 6.79917e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.375571, Final residual = 6.82163e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0198937, Final residual = 4.03299e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000193158, Final residual = 7.00079e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0694286, Final residual = 8.14067e-07, No Iterations 4 T gas min/max = 391.29, 433 DICPCG: Solving for p, Initial residual = 0.946043, Final residual = 0.0714164, No Iterations 50 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000390364, global = 1.66881e-08, cumulative = 3.47118e-06 DICPCG: Solving for p, Initial residual = 0.655004, Final residual = 8.84514e-07, No Iterations 122 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 6.86379e-10, global = 6.45033e-14, cumulative = 3.47118e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0599363, Final residual = 2.88966e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0255362, Final residual = 1.21247e-06, No Iterations 4 Mean pressure:119045 Mean temperature:396.278 Mean u':0.442861 ExecutionTime = 1460.26 s ClockTime = 1501 s Courant Number mean: 0.00280034 max: 0.0184164 deltaT = 0.000761935 Crank angle = -127.286 CA-deg deltaZ = 0.000334285 clearance: 0.0888896 Piston speed = 0.438731 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.198103, Final residual = 4.96584e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.190308, Final residual = 5.04637e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0163385, Final residual = 2.53328e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000187994, Final residual = 6.99746e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0703405, Final residual = 8.08493e-07, No Iterations 4 T gas min/max = 391.863, 433 DICPCG: Solving for p, Initial residual = 0.952495, Final residual = 0.0839591, No Iterations 43 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00046447, global = 2.83072e-08, cumulative = 3.49948e-06 DICPCG: Solving for p, Initial residual = 0.671344, Final residual = 8.54835e-07, No Iterations 116 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 7.23006e-10, global = -5.03483e-14, cumulative = 3.49948e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0589933, Final residual = 2.80177e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0250729, Final residual = 1.1721e-06, No Iterations 4 Mean pressure:119676 Mean temperature:396.885 Mean u':0.439055 ExecutionTime = 1474.91 s ClockTime = 1515 s Courant Number mean: 0.00285779 max: 0.0189432 deltaT = 0.000761935 Crank angle = -126.524 CA-deg deltaZ = 0.000339918 clearance: 0.0885497 Piston speed = 0.446125 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.244549, Final residual = 5.57057e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.24186, Final residual = 4.49607e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0170237, Final residual = 2.94822e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000185372, Final residual = 6.82442e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.071407, Final residual = 8.05521e-07, No Iterations 4 T gas min/max = 392.447, 433 DICPCG: Solving for p, Initial residual = 0.950873, Final residual = 0.088195, No Iterations 44 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000498215, global = 7.54821e-08, cumulative = 3.57497e-06 DICPCG: Solving for p, Initial residual = 0.680147, Final residual = 9.85191e-07, No Iterations 118 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 8.89097e-10, global = -1.01881e-15, cumulative = 3.57497e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0580353, Final residual = 2.71389e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0246195, Final residual = 1.13213e-06, No Iterations 4 Mean pressure:120322 Mean temperature:397.502 Mean u':0.435338 ExecutionTime = 1489.64 s ClockTime = 1530 s Courant Number mean: 0.00283263 max: 0.0165365 deltaT = 0.000761935 Crank angle = -125.762 CA-deg deltaZ = 0.000345569 clearance: 0.0882041 Piston speed = 0.453542 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.398562, Final residual = 6.78663e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.378932, Final residual = 5.88009e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0192228, Final residual = 3.04453e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000185642, Final residual = 9.40734e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0725411, Final residual = 8.0276e-07, No Iterations 4 T gas min/max = 393.043, 433 DICPCG: Solving for p, Initial residual = 0.949092, Final residual = 0.0670243, No Iterations 50 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000386699, global = 1.42996e-08, cumulative = 3.58927e-06 DICPCG: Solving for p, Initial residual = 0.622424, Final residual = 9.57366e-07, No Iterations 119 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 7.65682e-10, global = 1.93619e-14, cumulative = 3.58927e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0570839, Final residual = 2.63066e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0241748, Final residual = 1.09453e-06, No Iterations 4 Mean pressure:120984 Mean temperature:398.131 Mean u':0.431708 ExecutionTime = 1504.37 s ClockTime = 1545 s Courant Number mean: 0.00294708 max: 0.0176943 deltaT = 0.000761935 Crank angle = -125 CA-deg deltaZ = 0.000351236 clearance: 0.0878529 Piston speed = 0.460979 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.182505, Final residual = 4.60504e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.174006, Final residual = 4.49124e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0181138, Final residual = 2.88362e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000186656, Final residual = 6.21365e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0737193, Final residual = 8.01603e-07, No Iterations 4 T gas min/max = 393.652, 433 DICPCG: Solving for p, Initial residual = 0.952331, Final residual = 0.0831463, No Iterations 43 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000487335, global = 2.86352e-08, cumulative = 3.6179e-06 DICPCG: Solving for p, Initial residual = 0.66142, Final residual = 9.09077e-07, No Iterations 119 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 8.11825e-10, global = 9.487e-14, cumulative = 3.6179e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0561291, Final residual = 2.54971e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0237423, Final residual = 1.05854e-06, No Iterations 4 Mean pressure:121663 Mean temperature:398.771 Mean u':0.428162 ExecutionTime = 1520.68 s ClockTime = 1567 s Courant Number mean: 0.00300737 max: 0.019402 deltaT = 0.000833367 Crank angle = -124.167 CA-deg deltaZ = 0.000390672 clearance: 0.0874622 Piston speed = 0.468787 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.273705, Final residual = 8.62653e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.265264, Final residual = 7.49877e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0151872, Final residual = 2.55681e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000194575, Final residual = 6.16568e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0819164, Final residual = 1.28227e-06, No Iterations 4 T gas min/max = 394.332, 433 DICPCG: Solving for p, Initial residual = 0.94864, Final residual = 0.0910686, No Iterations 49 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000597506, global = 1.99234e-08, cumulative = 3.63782e-06 DICPCG: Solving for p, Initial residual = 0.705071, Final residual = 9.22751e-07, No Iterations 112 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 9.78149e-10, global = 7.171e-14, cumulative = 3.63782e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0594792, Final residual = 3.71254e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0253684, Final residual = 1.5597e-06, No Iterations 4 Mean pressure:122425 Mean temperature:399.484 Mean u':0.424387 ExecutionTime = 1535.37 s ClockTime = 1582 s Courant Number mean: 0.00332013 max: 0.0191279 deltaT = 0.000833367 Crank angle = -123.333 CA-deg deltaZ = 0.000397487 clearance: 0.0870647 Piston speed = 0.476966 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.249188, Final residual = 8.11317e-07, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.242603, Final residual = 8.51539e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0227908, Final residual = 5.05912e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000195241, Final residual = 9.41932e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0833238, Final residual = 1.28003e-06, No Iterations 4 T gas min/max = 395.026, 433 DICPCG: Solving for p, Initial residual = 0.949276, Final residual = 0.0875037, No Iterations 44 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000585562, global = 8.34002e-08, cumulative = 3.72122e-06 DICPCG: Solving for p, Initial residual = 0.684751, Final residual = 9.2872e-07, No Iterations 117 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 9.98168e-10, global = -3.87242e-14, cumulative = 3.72122e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0583917, Final residual = 3.59236e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0248794, Final residual = 1.50578e-06, No Iterations 4 Mean pressure:123208 Mean temperature:400.21 Mean u':0.420705 ExecutionTime = 1550.07 s ClockTime = 1597 s Courant Number mean: 0.00344637 max: 0.020192 deltaT = 0.000833367 Crank angle = -122.5 CA-deg deltaZ = 0.000404319 clearance: 0.0866604 Piston speed = 0.485164 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.383641, Final residual = 1.00867e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.370373, Final residual = 1.01937e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0133565, Final residual = 3.04529e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000194565, Final residual = 6.99178e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.084846, Final residual = 1.27994e-06, No Iterations 4 T gas min/max = 395.736, 433 DICPCG: Solving for p, Initial residual = 0.949539, Final residual = 0.0929143, No Iterations 50 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000634486, global = 7.02914e-08, cumulative = 3.79152e-06 DICPCG: Solving for p, Initial residual = 0.712768, Final residual = 7.93646e-07, No Iterations 130 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 9.07975e-10, global = -5.62061e-14, cumulative = 3.79152e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0573508, Final residual = 3.47938e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0243853, Final residual = 1.45298e-06, No Iterations 4 Mean pressure:124012 Mean temperature:400.951 Mean u':0.417117 ExecutionTime = 1564.86 s ClockTime = 1611 s Courant Number mean: 0.00344285 max: 0.0221991 deltaT = 0.000833367 Crank angle = -121.667 CA-deg deltaZ = 0.000411166 clearance: 0.0862492 Piston speed = 0.493379 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.349655, Final residual = 1.27376e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.343203, Final residual = 1.23756e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0317525, Final residual = 6.86558e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000195559, Final residual = 5.6581e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0864369, Final residual = 1.28177e-06, No Iterations 4 T gas min/max = 396.462, 433 DICPCG: Solving for p, Initial residual = 0.946962, Final residual = 0.0907017, No Iterations 51 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000633906, global = 5.47686e-08, cumulative = 3.84628e-06 DICPCG: Solving for p, Initial residual = 0.718164, Final residual = 9.89714e-07, No Iterations 130 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.17198e-09, global = 2.61916e-13, cumulative = 3.84629e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0562634, Final residual = 3.36952e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0239152, Final residual = 1.40548e-06, No Iterations 4 Mean pressure:124838 Mean temperature:401.707 Mean u':0.413617 ExecutionTime = 1579.67 s ClockTime = 1626 s Courant Number mean: 0.00363434 max: 0.0234874 deltaT = 0.000833367 Crank angle = -120.833 CA-deg deltaZ = 0.000418024 clearance: 0.0858312 Piston speed = 0.501609 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.314272, Final residual = 9.39103e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.303169, Final residual = 8.11509e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0117448, Final residual = 1.57793e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000192116, Final residual = 6.1069e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0880849, Final residual = 1.28603e-06, No Iterations 4 T gas min/max = 397.205, 433 DICPCG: Solving for p, Initial residual = 0.948846, Final residual = 0.0934868, No Iterations 45 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000665494, global = 1.07337e-07, cumulative = 3.95362e-06 DICPCG: Solving for p, Initial residual = 0.714263, Final residual = 6.90087e-07, No Iterations 131 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 8.25731e-10, global = 1.27992e-13, cumulative = 3.95362e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0552326, Final residual = 3.26401e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0234405, Final residual = 1.35722e-06, No Iterations 4 Mean pressure:125687 Mean temperature:402.478 Mean u':0.410206 ExecutionTime = 1594.38 s ClockTime = 1641 s Courant Number mean: 0.00364095 max: 0.0216339 deltaT = 0.000833367 Crank angle = -120 CA-deg deltaZ = 0.000424893 clearance: 0.0854063 Piston speed = 0.509852 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.401896, Final residual = 1.05599e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.386295, Final residual = 8.89152e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0353686, Final residual = 8.40306e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000193626, Final residual = 6.27112e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0897882, Final residual = 1.2898e-06, No Iterations 4 T gas min/max = 397.963, 433 DICPCG: Solving for p, Initial residual = 0.947787, Final residual = 0.0945836, No Iterations 51 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000687851, global = 8.86756e-08, cumulative = 4.0423e-06 DICPCG: Solving for p, Initial residual = 0.713537, Final residual = 9.72115e-07, No Iterations 123 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.19798e-09, global = -4.11572e-14, cumulative = 4.0423e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0541472, Final residual = 3.15993e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0229935, Final residual = 1.3137e-06, No Iterations 4 Mean pressure:126560 Mean temperature:403.264 Mean u':0.406877 ExecutionTime = 1610.79 s ClockTime = 1665 s Courant Number mean: 0.00393443 max: 0.0228047 deltaT = 0.00100004 Crank angle = -119 CA-deg deltaZ = 0.00051895 clearance: 0.0848873 Piston speed = 0.518929 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.370405, Final residual = 2.49651e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.355994, Final residual = 1.78604e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0140744, Final residual = 4.57473e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000221423, Final residual = 6.69619e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.109707, Final residual = 3.28029e-06, No Iterations 4 T gas min/max = 398.893, 433 DICPCG: Solving for p, Initial residual = 0.944982, Final residual = 0.093657, No Iterations 53 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000836776, global = 6.68123e-08, cumulative = 4.10911e-06 DICPCG: Solving for p, Initial residual = 0.735012, Final residual = 8.63032e-07, No Iterations 120 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.3162e-09, global = 1.20279e-13, cumulative = 4.10911e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0617196, Final residual = 6.80879e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0267351, Final residual = 2.91455e-06, No Iterations 4 Mean pressure:127637 Mean temperature:404.226 Mean u':0.403014 ExecutionTime = 1625.56 s ClockTime = 1679 s Courant Number mean: 0.00462328 max: 0.0274471 deltaT = 0.000800032 Crank angle = -118.2 CA-deg deltaZ = 0.000422297 clearance: 0.0844651 Piston speed = 0.52785 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.301779, Final residual = 7.93837e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.282632, Final residual = 6.08574e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0273518, Final residual = 5.54097e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000184414, Final residual = 5.61949e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.089776, Final residual = 1.04951e-06, No Iterations 4 T gas min/max = 399.656, 433 DICPCG: Solving for p, Initial residual = 0.951955, Final residual = 0.0838587, No Iterations 50 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000608763, global = 5.67784e-08, cumulative = 4.16589e-06 DICPCG: Solving for p, Initial residual = 0.682351, Final residual = 9.91624e-07, No Iterations 119 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.15289e-09, global = -5.65229e-14, cumulative = 4.16589e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0502006, Final residual = 2.45444e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0211866, Final residual = 1.00872e-06, No Iterations 4 Mean pressure:128526 Mean temperature:405.013 Mean u':0.399983 ExecutionTime = 1640.26 s ClockTime = 1694 s Courant Number mean: 0.00391177 max: 0.0228569 deltaT = 0.000800032 Crank angle = -117.4 CA-deg deltaZ = 0.000428643 clearance: 0.0840364 Piston speed = 0.535782 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.266216, Final residual = 6.35725e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.261053, Final residual = 5.62738e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0111698, Final residual = 1.70128e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000184896, Final residual = 1.06926e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0917286, Final residual = 1.0578e-06, No Iterations 4 T gas min/max = 400.437, 433 DICPCG: Solving for p, Initial residual = 0.95098, Final residual = 0.0938852, No Iterations 44 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000695884, global = 1.33551e-07, cumulative = 4.29944e-06 DICPCG: Solving for p, Initial residual = 0.714381, Final residual = 8.61627e-07, No Iterations 120 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.03861e-09, global = -7.39667e-14, cumulative = 4.29944e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0492582, Final residual = 2.38056e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0207798, Final residual = 9.77017e-07, No Iterations 4 Mean pressure:129438 Mean temperature:405.818 Mean u':0.397025 ExecutionTime = 1654.95 s ClockTime = 1709 s Courant Number mean: 0.00383242 max: 0.0239403 deltaT = 0.000800032 Crank angle = -116.6 CA-deg deltaZ = 0.000434989 clearance: 0.0836014 Piston speed = 0.543714 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.409832, Final residual = 8.72907e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.379451, Final residual = 7.76217e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0358538, Final residual = 6.62089e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000181621, Final residual = 7.51184e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.093581, Final residual = 1.06449e-06, No Iterations 4 T gas min/max = 401.236, 433 DICPCG: Solving for p, Initial residual = 0.948745, Final residual = 0.0897674, No Iterations 51 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000679867, global = 7.98537e-08, cumulative = 4.37929e-06 DICPCG: Solving for p, Initial residual = 0.708508, Final residual = 7.4074e-07, No Iterations 129 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 8.9778e-10, global = 9.62024e-14, cumulative = 4.37929e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0482932, Final residual = 2.30806e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0203987, Final residual = 9.47718e-07, No Iterations 4 Mean pressure:130375 Mean temperature:406.638 Mean u':0.394135 ExecutionTime = 1669.7 s ClockTime = 1724 s Courant Number mean: 0.004137 max: 0.0270689 deltaT = 0.000800032 Crank angle = -115.8 CA-deg deltaZ = 0.000441333 clearance: 0.0831601 Piston speed = 0.551644 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.301286, Final residual = 6.19102e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.313662, Final residual = 6.80326e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.00935887, Final residual = 1.37667e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000184701, Final residual = 4.47477e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0954455, Final residual = 1.07153e-06, No Iterations 4 T gas min/max = 402.051, 433 DICPCG: Solving for p, Initial residual = 0.951803, Final residual = 0.0726234, No Iterations 50 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000558767, global = 4.52903e-08, cumulative = 4.42458e-06 DICPCG: Solving for p, Initial residual = 0.66532, Final residual = 8.03933e-07, No Iterations 129 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 8.90162e-10, global = 1.4127e-13, cumulative = 4.42458e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0474049, Final residual = 2.24063e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0200116, Final residual = 9.75531e-06, No Iterations 3 Mean pressure:131337 Mean temperature:407.475 Mean u':0.391313 ExecutionTime = 1684.47 s ClockTime = 1738 s Courant Number mean: 0.00410058 max: 0.0274491 deltaT = 0.000800032 Crank angle = -115 CA-deg deltaZ = 0.000447673 clearance: 0.0827124 Piston speed = 0.559568 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.233521, Final residual = 6.29394e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.230831, Final residual = 5.56545e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0249343, Final residual = 4.59944e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000181636, Final residual = 3.81764e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0973576, Final residual = 1.07859e-06, No Iterations 4 T gas min/max = 402.883, 433 DICPCG: Solving for p, Initial residual = 0.952728, Final residual = 0.0940682, No Iterations 50 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000736826, global = 5.52571e-08, cumulative = 4.47984e-06 DICPCG: Solving for p, Initial residual = 0.722519, Final residual = 9.25869e-07, No Iterations 119 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.197e-09, global = 3.95135e-14, cumulative = 4.47984e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0464936, Final residual = 2.17625e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0196395, Final residual = 9.5229e-06, No Iterations 3 Mean pressure:132324 Mean temperature:408.327 Mean u':0.388555 ExecutionTime = 1700.86 s ClockTime = 1765 s Courant Number mean: 0.00430112 max: 0.0269453 deltaT = 0.000833367 Crank angle = -114.167 CA-deg deltaZ = 0.000473059 clearance: 0.0822394 Piston speed = 0.567649 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.280936, Final residual = 9.5902e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.273305, Final residual = 8.22656e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0110255, Final residual = 1.67434e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000190688, Final residual = 7.02028e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.10344, Final residual = 1.34745e-06, No Iterations 4 T gas min/max = 403.769, 433 DICPCG: Solving for p, Initial residual = 0.94994, Final residual = 0.0892313, No Iterations 45 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000744056, global = 1.18062e-07, cumulative = 4.5979e-06 DICPCG: Solving for p, Initial residual = 0.721666, Final residual = 9.05665e-07, No Iterations 129 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.20735e-09, global = -1.7524e-14, cumulative = 4.5979e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0472259, Final residual = 2.54947e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.020015, Final residual = 1.04544e-06, No Iterations 4 Mean pressure:133381 Mean temperature:409.233 Mean u':0.385757 ExecutionTime = 1715.57 s ClockTime = 1780 s Courant Number mean: 0.00443113 max: 0.0264272 deltaT = 0.000833367 Crank angle = -113.333 CA-deg deltaZ = 0.00047992 clearance: 0.0817594 Piston speed = 0.575881 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.363697, Final residual = 8.84551e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.346279, Final residual = 7.44572e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0352274, Final residual = 7.61747e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000192876, Final residual = 2.34482e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.10559, Final residual = 1.35873e-06, No Iterations 4 T gas min/max = 404.673, 433 DICPCG: Solving for p, Initial residual = 0.949872, Final residual = 0.0798075, No Iterations 52 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000678489, global = 6.17095e-08, cumulative = 4.65961e-06 DICPCG: Solving for p, Initial residual = 0.696825, Final residual = 9.81622e-07, No Iterations 128 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.2684e-09, global = 7.30677e-14, cumulative = 4.65961e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0462484, Final residual = 2.47495e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0196281, Final residual = 1.0172e-06, No Iterations 4 Mean pressure:134466 Mean temperature:410.156 Mean u':0.383024 ExecutionTime = 1730.33 s ClockTime = 1795 s Courant Number mean: 0.00476475 max: 0.0277448 deltaT = 0.000833367 Crank angle = -112.5 CA-deg deltaZ = 0.000486766 clearance: 0.0812727 Piston speed = 0.584096 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.294839, Final residual = 8.94521e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.274998, Final residual = 6.22687e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.00912957, Final residual = 1.61129e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000189101, Final residual = 8.69909e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.107852, Final residual = 1.37439e-06, No Iterations 4 T gas min/max = 405.597, 433.38 DICPCG: Solving for p, Initial residual = 0.953444, Final residual = 0.0947435, No Iterations 49 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000818088, global = 4.95884e-08, cumulative = 4.7092e-06 DICPCG: Solving for p, Initial residual = 0.727512, Final residual = 8.00493e-07, No Iterations 118 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.12098e-09, global = -3.11194e-14, cumulative = 4.7092e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0453397, Final residual = 2.40485e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0192342, Final residual = 9.8692e-07, No Iterations 4 Mean pressure:135583 Mean temperature:411.097 Mean u':0.380359 ExecutionTime = 1745.02 s ClockTime = 1809 s Courant Number mean: 0.0047302 max: 0.0280449 deltaT = 0.000833367 Crank angle = -111.667 CA-deg deltaZ = 0.000493595 clearance: 0.0807791 Piston speed = 0.59229 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.260074, Final residual = 9.15087e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.253068, Final residual = 8.802e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0251621, Final residual = 5.38739e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000193198, Final residual = 4.81508e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.110201, Final residual = 1.38916e-06, No Iterations 4 T gas min/max = 406.54, 434.033 DICPCG: Solving for p, Initial residual = 0.951217, Final residual = 0.0860831, No Iterations 51 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000759515, global = 3.05015e-08, cumulative = 4.7397e-06 DICPCG: Solving for p, Initial residual = 0.718373, Final residual = 9.52541e-07, No Iterations 120 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.29818e-09, global = 1.23111e-13, cumulative = 4.7397e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0444094, Final residual = 2.33757e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0188537, Final residual = 9.59064e-07, No Iterations 4 Mean pressure:136730 Mean temperature:412.058 Mean u':0.377757 ExecutionTime = 1759.7 s ClockTime = 1824 s Courant Number mean: 0.00495622 max: 0.0285952 deltaT = 0.000833367 Crank angle = -110.833 CA-deg deltaZ = 0.000500403 clearance: 0.0802787 Piston speed = 0.60046 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.210221, Final residual = 6.96725e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.216051, Final residual = 5.29423e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0114012, Final residual = 1.78041e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000188677, Final residual = 4.74751e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.112631, Final residual = 1.40779e-06, No Iterations 4 T gas min/max = 407.505, 434.692 DICPCG: Solving for p, Initial residual = 0.952522, Final residual = 0.0914734, No Iterations 42 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000821548, global = 9.023e-08, cumulative = 4.82993e-06 DICPCG: Solving for p, Initial residual = 0.744393, Final residual = 8.55818e-07, No Iterations 118 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.24255e-09, global = 1.21811e-13, cumulative = 4.82993e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.043522, Final residual = 2.27262e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0184681, Final residual = 9.82442e-06, No Iterations 3 Mean pressure:137910 Mean temperature:413.037 Mean u':0.37522 ExecutionTime = 1774.37 s ClockTime = 1839 s Courant Number mean: 0.00493059 max: 0.028669 deltaT = 0.000833367 Crank angle = -110 CA-deg deltaZ = 0.000507187 clearance: 0.0797715 Piston speed = 0.6086 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.265938, Final residual = 7.90752e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.25384, Final residual = 5.91267e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0269956, Final residual = 5.03711e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000186367, Final residual = 5.51693e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.115145, Final residual = 1.42643e-06, No Iterations 4 T gas min/max = 408.49, 435.359 DICPCG: Solving for p, Initial residual = 0.951134, Final residual = 0.0787649, No Iterations 52 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00072207, global = 3.43558e-08, cumulative = 4.86429e-06 DICPCG: Solving for p, Initial residual = 0.702215, Final residual = 8.39778e-07, No Iterations 118 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.1307e-09, global = -1.11602e-13, cumulative = 4.86429e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0425946, Final residual = 2.2071e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0181032, Final residual = 9.59401e-06, No Iterations 3 Mean pressure:139123 Mean temperature:414.037 Mean u':0.372742 ExecutionTime = 1790.66 s ClockTime = 1858 s Courant Number mean: 0.00511925 max: 0.0300714 deltaT = 0.00100004 Crank angle = -109 CA-deg deltaZ = 0.00061754 clearance: 0.0791539 Piston speed = 0.617516 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.28838, Final residual = 1.40277e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.287586, Final residual = 1.39847e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0110662, Final residual = 2.50962e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000215187, Final residual = 1.86179e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.141068, Final residual = 3.66419e-06, No Iterations 4 T gas min/max = 409.696, 436.178 DICPCG: Solving for p, Initial residual = 0.949825, Final residual = 0.0921674, No Iterations 50 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00103479, global = 4.88237e-08, cumulative = 4.91311e-06 DICPCG: Solving for p, Initial residual = 0.736213, Final residual = 8.3477e-07, No Iterations 131 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.47663e-09, global = 9.46998e-14, cumulative = 4.91311e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0485022, Final residual = 4.81693e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0210343, Final residual = 2.0239e-06, No Iterations 4 Mean pressure:140623 Mean temperature:415.259 Mean u':0.369867 ExecutionTime = 1805.47 s ClockTime = 1873 s Courant Number mean: 0.00618293 max: 0.0362333 deltaT = 0.000800032 Crank angle = -108.2 CA-deg deltaZ = 0.000501 clearance: 0.0786529 Piston speed = 0.626225 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.234738, Final residual = 6.12787e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.255324, Final residual = 5.35568e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0253439, Final residual = 4.33146e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000181926, Final residual = 3.16568e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.115893, Final residual = 1.18632e-06, No Iterations 4 T gas min/max = 410.685, 436.851 DICPCG: Solving for p, Initial residual = 0.95627, Final residual = 0.0808315, No Iterations 51 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000737112, global = 3.39376e-08, cumulative = 4.94705e-06 DICPCG: Solving for p, Initial residual = 0.698049, Final residual = 9.31363e-07, No Iterations 118 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.23547e-09, global = -5.62157e-14, cumulative = 4.94705e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0393114, Final residual = 1.72638e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0166424, Final residual = 7.79664e-06, No Iterations 3 Mean pressure:141860 Mean temperature:416.259 Mean u':0.367611 ExecutionTime = 1820.23 s ClockTime = 1888 s Courant Number mean: 0.00511012 max: 0.030791 deltaT = 0.000800032 Crank angle = -107.4 CA-deg deltaZ = 0.00050716 clearance: 0.0781458 Piston speed = 0.633924 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.277745, Final residual = 5.6919e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.285531, Final residual = 4.51876e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0088775, Final residual = 9.77422e-07, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000181546, Final residual = 5.74784e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.118739, Final residual = 1.20701e-06, No Iterations 4 T gas min/max = 411.697, 437.535 DICPCG: Solving for p, Initial residual = 0.95493, Final residual = 0.0865013, No Iterations 45 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000804785, global = 7.04669e-08, cumulative = 5.01752e-06 DICPCG: Solving for p, Initial residual = 0.721468, Final residual = 9.7574e-07, No Iterations 127 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.36331e-09, global = 7.8491e-16, cumulative = 5.01752e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0385066, Final residual = 1.6834e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0163053, Final residual = 7.61636e-06, No Iterations 3 Mean pressure:143131 Mean temperature:417.281 Mean u':0.36541 ExecutionTime = 1834.96 s ClockTime = 1903 s Courant Number mean: 0.00510352 max: 0.0307276 deltaT = 0.000800032 Crank angle = -106.6 CA-deg deltaZ = 0.000513284 clearance: 0.0776325 Piston speed = 0.64158 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.270318, Final residual = 4.09327e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.279874, Final residual = 5.27752e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0262778, Final residual = 4.57426e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000178847, Final residual = 7.16754e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.12148, Final residual = 1.22908e-06, No Iterations 4 T gas min/max = 412.731, 438.228 DICPCG: Solving for p, Initial residual = 0.953764, Final residual = 0.0783841, No Iterations 50 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000743495, global = 5.66209e-08, cumulative = 5.07414e-06 DICPCG: Solving for p, Initial residual = 0.69755, Final residual = 8.33725e-07, No Iterations 123 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.11665e-09, global = 2.77062e-14, cumulative = 5.07414e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0376897, Final residual = 1.63922e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0159847, Final residual = 7.45181e-06, No Iterations 3 Mean pressure:144438 Mean temperature:418.323 Mean u':0.363259 ExecutionTime = 1849.74 s ClockTime = 1918 s Courant Number mean: 0.00538064 max: 0.0322086 deltaT = 0.000800032 Crank angle = -105.8 CA-deg deltaZ = 0.00051937 clearance: 0.0771131 Piston speed = 0.649187 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.234225, Final residual = 4.86416e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.252343, Final residual = 3.72593e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.00794015, Final residual = 1.17961e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000181066, Final residual = 6.64203e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.124256, Final residual = 1.25017e-06, No Iterations 4 T gas min/max = 413.785, 438.93 DICPCG: Solving for p, Initial residual = 0.956101, Final residual = 0.0777476, No Iterations 49 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000748938, global = 3.95147e-08, cumulative = 5.11365e-06 DICPCG: Solving for p, Initial residual = 0.700409, Final residual = 8.71817e-07, No Iterations 122 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.16736e-09, global = -1.38917e-13, cumulative = 5.11365e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0369265, Final residual = 1.59753e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.015659, Final residual = 7.27977e-06, No Iterations 3 Mean pressure:145781 Mean temperature:419.386 Mean u':0.361159 ExecutionTime = 1864.44 s ClockTime = 1932 s Courant Number mean: 0.0053365 max: 0.0323498 deltaT = 0.000800032 Crank angle = -105 CA-deg deltaZ = 0.000525414 clearance: 0.0765877 Piston speed = 0.656741 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.1898, Final residual = 3.00065e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.187515, Final residual = 2.96973e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0201666, Final residual = 3.57289e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000180877, Final residual = 4.96206e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.12711, Final residual = 1.2702e-06, No Iterations 4 T gas min/max = 414.862, 439.641 DICPCG: Solving for p, Initial residual = 0.957136, Final residual = 0.0894145, No Iterations 50 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000875828, global = 3.95892e-08, cumulative = 5.15324e-06 DICPCG: Solving for p, Initial residual = 0.729354, Final residual = 9.05246e-07, No Iterations 117 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.3175e-09, global = -1.11248e-13, cumulative = 5.15324e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0361527, Final residual = 1.55797e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0153408, Final residual = 7.11986e-06, No Iterations 3 Mean pressure:147160 Mean temperature:420.469 Mean u':0.359109 ExecutionTime = 1880.7 s ClockTime = 1954 s Courant Number mean: 0.00553263 max: 0.0335901 deltaT = 0.000833367 Crank angle = -104.167 CA-deg deltaZ = 0.000553684 clearance: 0.076034 Piston speed = 0.664394 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.219866, Final residual = 5.03421e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.216626, Final residual = 4.44494e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0100124, Final residual = 1.45157e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000185135, Final residual = 2.08318e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.135426, Final residual = 1.60051e-06, No Iterations 4 T gas min/max = 416.006, 440.418 DICPCG: Solving for p, Initial residual = 0.955289, Final residual = 0.0848385, No Iterations 45 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000882753, global = 8.35163e-08, cumulative = 5.23676e-06 DICPCG: Solving for p, Initial residual = 0.727587, Final residual = 8.87961e-07, No Iterations 129 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.32591e-09, global = -6.03729e-14, cumulative = 5.23676e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0366451, Final residual = 1.82888e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0156068, Final residual = 8.12075e-06, No Iterations 3 Mean pressure:148638 Mean temperature:421.619 Mean u':0.35703 ExecutionTime = 1895.39 s ClockTime = 1969 s Courant Number mean: 0.00567227 max: 0.0353289 deltaT = 0.000833367 Crank angle = -103.333 CA-deg deltaZ = 0.000560136 clearance: 0.0754739 Piston speed = 0.672137 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.254799, Final residual = 6.45458e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.249895, Final residual = 5.46104e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0297895, Final residual = 5.99567e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000187142, Final residual = 9.78695e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.138662, Final residual = 1.63026e-06, No Iterations 4 T gas min/max = 417.174, 441.383 DICPCG: Solving for p, Initial residual = 0.955353, Final residual = 0.0842964, No Iterations 50 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000893161, global = 3.38098e-08, cumulative = 5.27057e-06 DICPCG: Solving for p, Initial residual = 0.721709, Final residual = 8.96148e-07, No Iterations 128 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.35092e-09, global = 1.03545e-13, cumulative = 5.27057e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0358064, Final residual = 1.78341e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0152712, Final residual = 7.94838e-06, No Iterations 3 Mean pressure:150158 Mean temperature:422.791 Mean u':0.355002 ExecutionTime = 1910.13 s ClockTime = 1984 s Courant Number mean: 0.00599033 max: 0.0366486 deltaT = 0.000833367 Crank angle = -102.5 CA-deg deltaZ = 0.000566529 clearance: 0.0749074 Piston speed = 0.679808 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.215928, Final residual = 5.22987e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.215775, Final residual = 5.01373e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0096949, Final residual = 1.58323e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000182867, Final residual = 1.66041e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.142061, Final residual = 1.66701e-06, No Iterations 4 T gas min/max = 418.366, 442.375 DICPCG: Solving for p, Initial residual = 0.957356, Final residual = 0.0912266, No Iterations 43 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000982287, global = 7.60534e-08, cumulative = 5.34662e-06 DICPCG: Solving for p, Initial residual = 0.746523, Final residual = 8.43936e-07, No Iterations 129 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.35851e-09, global = -3.48177e-14, cumulative = 5.34662e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0350108, Final residual = 1.73872e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0149301, Final residual = 7.75983e-06, No Iterations 3 Mean pressure:151722 Mean temperature:423.987 Mean u':0.353026 ExecutionTime = 1924.82 s ClockTime = 1999 s Courant Number mean: 0.00592348 max: 0.0379809 deltaT = 0.000833367 Crank angle = -101.667 CA-deg deltaZ = 0.000572858 clearance: 0.0743345 Piston speed = 0.687402 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.278329, Final residual = 5.79788e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.280781, Final residual = 5.41687e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0212274, Final residual = 3.67683e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000186123, Final residual = 2.01865e-06, No Iterations 3 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.145599, Final residual = 1.70179e-06, No Iterations 4 T gas min/max = 419.583, 443.381 DICPCG: Solving for p, Initial residual = 0.956029, Final residual = 0.0881227, No Iterations 50 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000967579, global = 9.05887e-08, cumulative = 5.43721e-06 DICPCG: Solving for p, Initial residual = 0.743133, Final residual = 9.81705e-07, No Iterations 118 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.61892e-09, global = 8.6078e-14, cumulative = 5.43721e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.034185, Final residual = 1.69384e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0146066, Final residual = 7.5964e-06, No Iterations 3 Mean pressure:153331 Mean temperature:425.206 Mean u':0.351098 ExecutionTime = 1939.45 s ClockTime = 2013 s Courant Number mean: 0.00626414 max: 0.0393515 deltaT = 0.000833367 Crank angle = -100.833 CA-deg deltaZ = 0.000579117 clearance: 0.0737554 Piston speed = 0.694912 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.282432, Final residual = 7.76244e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.282498, Final residual = 5.02877e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.00935713, Final residual = 1.79674e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000184924, Final residual = 1.17957e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.149268, Final residual = 1.73954e-06, No Iterations 4 T gas min/max = 420.827, 444.401 DICPCG: Solving for p, Initial residual = 0.956629, Final residual = 0.0947316, No Iterations 49 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00105844, global = 7.66947e-08, cumulative = 5.5139e-06 DICPCG: Solving for p, Initial residual = 0.761179, Final residual = 8.45066e-07, No Iterations 129 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.47407e-09, global = 1.625e-14, cumulative = 5.5139e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0334377, Final residual = 1.65494e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0142675, Final residual = 7.41642e-06, No Iterations 3 Mean pressure:154988 Mean temperature:426.45 Mean u':0.349221 ExecutionTime = 1954.19 s ClockTime = 2028 s Courant Number mean: 0.00628614 max: 0.0393114 deltaT = 0.000833367 Crank angle = -100 CA-deg deltaZ = 0.000585303 clearance: 0.0731701 Piston speed = 0.702335 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.28628, Final residual = 7.61297e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.284711, Final residual = 4.93676e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0239882, Final residual = 4.51164e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000183842, Final residual = 4.31044e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.153076, Final residual = 1.78032e-06, No Iterations 4 T gas min/max = 422.096, 445.436 DICPCG: Solving for p, Initial residual = 0.956051, Final residual = 0.07056, No Iterations 53 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00080315, global = 1.35983e-08, cumulative = 5.5275e-06 DICPCG: Solving for p, Initial residual = 0.689791, Final residual = 8.5357e-07, No Iterations 129 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.24787e-09, global = 6.703e-14, cumulative = 5.5275e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0326495, Final residual = 1.61583e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0139454, Final residual = 7.25741e-06, No Iterations 3 Mean pressure:156693 Mean temperature:427.719 Mean u':0.347392 ExecutionTime = 1970.63 s ClockTime = 2049 s Courant Number mean: 0.00646877 max: 0.0405038 deltaT = 0.00100004 Crank angle = -99 CA-deg deltaZ = 0.000710418 clearance: 0.0724597 Piston speed = 0.71039 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.220076, Final residual = 9.43006e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.218712, Final residual = 7.53337e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0103436, Final residual = 2.74626e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000209552, Final residual = 6.34372e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.187845, Final residual = 4.59195e-06, No Iterations 4 T gas min/max = 423.65, 446.69 DICPCG: Solving for p, Initial residual = 0.956543, Final residual = 0.0840841, No Iterations 46 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00116821, global = 4.70232e-08, cumulative = 5.57453e-06 DICPCG: Solving for p, Initial residual = 0.732772, Final residual = 8.43003e-07, No Iterations 130 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.65082e-09, global = 5.86164e-14, cumulative = 5.57453e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0370471, Final residual = 3.53202e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0161575, Final residual = 1.46605e-06, No Iterations 4 Mean pressure:158803 Mean temperature:429.269 Mean u':0.345271 ExecutionTime = 1985.37 s ClockTime = 2064 s Courant Number mean: 0.00778173 max: 0.0504172 deltaT = 0.000800032 Crank angle = -98.2 CA-deg deltaZ = 0.000574571 clearance: 0.0718851 Piston speed = 0.718185 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.210365, Final residual = 4.2034e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.213486, Final residual = 4.46264e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.015484, Final residual = 2.73275e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000176508, Final residual = 4.05981e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.155205, Final residual = 1.51809e-06, No Iterations 4 T gas min/max = 424.923, 447.714 DICPCG: Solving for p, Initial residual = 0.961819, Final residual = 0.0944459, No Iterations 48 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00106631, global = 7.76686e-08, cumulative = 5.65219e-06 DICPCG: Solving for p, Initial residual = 0.75396, Final residual = 7.19738e-07, No Iterations 128 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.23256e-09, global = -8.24142e-14, cumulative = 5.65219e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0299541, Final residual = 1.27516e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0127379, Final residual = 5.92017e-06, No Iterations 3 Mean pressure:160547 Mean temperature:430.539 Mean u':0.34361 ExecutionTime = 2000.07 s ClockTime = 2079 s Courant Number mean: 0.00658994 max: 0.0411997 deltaT = 0.000800032 Crank angle = -97.4 CA-deg deltaZ = 0.000580029 clearance: 0.0713051 Piston speed = 0.725008 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.224928, Final residual = 4.96894e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.230155, Final residual = 5.01756e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.00828319, Final residual = 1.26554e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000175915, Final residual = 4.52093e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.159488, Final residual = 1.56019e-06, No Iterations 4 T gas min/max = 426.225, 448.802 DICPCG: Solving for p, Initial residual = 0.957995, Final residual = 0.0910238, No Iterations 48 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00105022, global = 7.65279e-08, cumulative = 5.72872e-06 DICPCG: Solving for p, Initial residual = 0.770408, Final residual = 7.72514e-07, No Iterations 122 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.33965e-09, global = -7.37978e-14, cumulative = 5.72872e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0292809, Final residual = 1.24566e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0124361, Final residual = 5.77663e-06, No Iterations 3 Mean pressure:162341 Mean temperature:431.836 Mean u':0.341994 ExecutionTime = 2014.81 s ClockTime = 2094 s Courant Number mean: 0.00644057 max: 0.0423426 deltaT = 0.000800032 Crank angle = -96.6 CA-deg deltaZ = 0.000585406 clearance: 0.0707197 Piston speed = 0.731728 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.304865, Final residual = 5.9568e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.312509, Final residual = 5.5322e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0223396, Final residual = 4.04732e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000176978, Final residual = 6.55322e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.163672, Final residual = 1.59883e-06, No Iterations 4 T gas min/max = 427.554, 449.975 DICPCG: Solving for p, Initial residual = 0.958617, Final residual = 0.0831877, No Iterations 52 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000975559, global = 1.51552e-08, cumulative = 5.74388e-06 DICPCG: Solving for p, Initial residual = 0.736008, Final residual = 8.35505e-07, No Iterations 128 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.35463e-09, global = 7.27197e-14, cumulative = 5.74388e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0285881, Final residual = 1.21989e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0121473, Final residual = 5.66817e-06, No Iterations 3 Mean pressure:164187 Mean temperature:433.159 Mean u':0.340419 ExecutionTime = 2029.49 s ClockTime = 2108 s Courant Number mean: 0.00680795 max: 0.0430941 deltaT = 0.000800032 Crank angle = -95.8 CA-deg deltaZ = 0.000590696 clearance: 0.070129 Piston speed = 0.738341 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.214005, Final residual = 4.16727e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.216919, Final residual = 3.2994e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.00701334, Final residual = 1.00219e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000177565, Final residual = 6.67217e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.167938, Final residual = 1.64755e-06, No Iterations 4 T gas min/max = 428.91, 451.164 DICPCG: Solving for p, Initial residual = 0.960442, Final residual = 0.0949326, No Iterations 44 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00113009, global = 6.89626e-08, cumulative = 5.81284e-06 DICPCG: Solving for p, Initial residual = 0.770019, Final residual = 7.61479e-07, No Iterations 116 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.33347e-09, global = 1.22118e-13, cumulative = 5.81284e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0279248, Final residual = 1.19274e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0118531, Final residual = 5.54156e-06, No Iterations 3 Mean pressure:166086 Mean temperature:434.507 Mean u':0.338885 ExecutionTime = 2044.1 s ClockTime = 2123 s Courant Number mean: 0.00683901 max: 0.0435413 deltaT = 0.000800032 Crank angle = -95 CA-deg deltaZ = 0.000595896 clearance: 0.0695331 Piston speed = 0.74484 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.239844, Final residual = 6.64402e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.23957, Final residual = 4.70773e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0160668, Final residual = 2.82073e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000178423, Final residual = 6.11295e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.172342, Final residual = 1.69144e-06, No Iterations 4 T gas min/max = 430.293, 452.371 DICPCG: Solving for p, Initial residual = 0.958861, Final residual = 0.0950315, No Iterations 50 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00115228, global = 3.83162e-08, cumulative = 5.85116e-06 DICPCG: Solving for p, Initial residual = 0.77039, Final residual = 9.21716e-07, No Iterations 117 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.65401e-09, global = 1.1703e-14, cumulative = 5.85116e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0272486, Final residual = 1.16674e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0115689, Final residual = 5.42274e-06, No Iterations 3 Mean pressure:168039 Mean temperature:435.881 Mean u':0.337391 ExecutionTime = 2060.34 s ClockTime = 2142 s Courant Number mean: 0.00703957 max: 0.0456533 deltaT = 0.000833367 Crank angle = -94.1667 CA-deg deltaZ = 0.000626152 clearance: 0.0689069 Piston speed = 0.751352 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.253505, Final residual = 4.60672e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.255361, Final residual = 4.47117e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0070861, Final residual = 1.42925e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000181872, Final residual = 7.4232e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.184133, Final residual = 2.15185e-06, No Iterations 4 T gas min/max = 431.762, 453.645 DICPCG: Solving for p, Initial residual = 0.959053, Final residual = 0.08948, No Iterations 47 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.0011488, global = 8.72742e-08, cumulative = 5.93843e-06 DICPCG: Solving for p, Initial residual = 0.776764, Final residual = 8.6627e-07, No Iterations 126 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.55805e-09, global = -3.29539e-14, cumulative = 5.93843e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0275339, Final residual = 1.37551e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.011714, Final residual = 6.18251e-06, No Iterations 3 Mean pressure:170134 Mean temperature:437.34 Mean u':0.335882 ExecutionTime = 2075 s ClockTime = 2156 s Courant Number mean: 0.00726977 max: 0.0472458 deltaT = 0.000833367 Crank angle = -93.3333 CA-deg deltaZ = 0.00063158 clearance: 0.0682753 Piston speed = 0.757866 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.249596, Final residual = 6.77943e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.249183, Final residual = 6.55109e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0278688, Final residual = 5.84694e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000181729, Final residual = 9.49032e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.189177, Final residual = 2.2184e-06, No Iterations 4 T gas min/max = 433, 454.94 DICPCG: Solving for p, Initial residual = 0.959941, Final residual = 0.0903818, No Iterations 50 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.0011794, global = 5.12051e-08, cumulative = 5.98964e-06 DICPCG: Solving for p, Initial residual = 0.778052, Final residual = 9.11593e-07, No Iterations 126 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.70577e-09, global = 7.05871e-14, cumulative = 5.98964e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.026804, Final residual = 1.34283e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0114078, Final residual = 6.04137e-06, No Iterations 3 Mean pressure:172292 Mean temperature:438.826 Mean u':0.334414 ExecutionTime = 2089.7 s ClockTime = 2171 s Courant Number mean: 0.00748806 max: 0.0497043 deltaT = 0.000833367 Crank angle = -92.5 CA-deg deltaZ = 0.000636891 clearance: 0.0676384 Piston speed = 0.764239 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.268771, Final residual = 8.52326e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.279431, Final residual = 7.69827e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.00848791, Final residual = 1.75314e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000179743, Final residual = 9.5989e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.19448, Final residual = 2.28814e-06, No Iterations 4 T gas min/max = 433, 456.252 DICPCG: Solving for p, Initial residual = 0.960159, Final residual = 0.0786833, No Iterations 46 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00104426, global = 4.48121e-08, cumulative = 6.03445e-06 DICPCG: Solving for p, Initial residual = 0.751749, Final residual = 9.28121e-07, No Iterations 127 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.61126e-09, global = 7.44718e-14, cumulative = 6.03445e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0261027, Final residual = 1.31378e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0110969, Final residual = 5.90432e-06, No Iterations 3 Mean pressure:174516 Mean temperature:440.342 Mean u':0.33299 ExecutionTime = 2104.36 s ClockTime = 2186 s Courant Number mean: 0.00749071 max: 0.0500983 deltaT = 0.000833367 Crank angle = -91.6667 CA-deg deltaZ = 0.000642081 clearance: 0.0669964 Piston speed = 0.770467 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.197846, Final residual = 3.56564e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.200663, Final residual = 4.23016e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0190707, Final residual = 3.95713e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000181291, Final residual = 4.267e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.200011, Final residual = 2.36462e-06, No Iterations 4 T gas min/max = 433, 457.608 DICPCG: Solving for p, Initial residual = 0.962785, Final residual = 0.0944006, No Iterations 49 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00127091, global = 5.38951e-08, cumulative = 6.08834e-06 DICPCG: Solving for p, Initial residual = 0.783334, Final residual = 9.776e-07, No Iterations 126 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.90646e-09, global = 6.61567e-14, cumulative = 6.08834e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0253881, Final residual = 1.28398e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0107929, Final residual = 5.77529e-06, No Iterations 3 Mean pressure:176808 Mean temperature:441.888 Mean u':0.331607 ExecutionTime = 2119.05 s ClockTime = 2201 s Courant Number mean: 0.00783784 max: 0.0509583 deltaT = 0.000833367 Crank angle = -90.8333 CA-deg deltaZ = 0.000647145 clearance: 0.0663492 Piston speed = 0.776543 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.231518, Final residual = 6.09607e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.233094, Final residual = 6.67899e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.00934421, Final residual = 2.07728e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000182545, Final residual = 6.79037e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.205766, Final residual = 2.44418e-06, No Iterations 4 T gas min/max = 433, 458.984 DICPCG: Solving for p, Initial residual = 0.960931, Final residual = 0.0928025, No Iterations 45 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00127354, global = 6.76099e-08, cumulative = 6.15595e-06 DICPCG: Solving for p, Initial residual = 0.794015, Final residual = 8.83756e-07, No Iterations 111 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.75325e-09, global = 1.59212e-13, cumulative = 6.15595e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0247031, Final residual = 1.2565e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0104827, Final residual = 5.63256e-06, No Iterations 3 Mean pressure:179170 Mean temperature:443.465 Mean u':0.330266 ExecutionTime = 2133.63 s ClockTime = 2215 s Courant Number mean: 0.00778324 max: 0.0516924 deltaT = 0.000833367 Crank angle = -90 CA-deg deltaZ = 0.000652077 clearance: 0.0656971 Piston speed = 0.782461 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.208733, Final residual = 4.78386e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.207105, Final residual = 5.57022e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0221231, Final residual = 4.64745e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000182028, Final residual = 4.25452e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.211758, Final residual = 2.53073e-06, No Iterations 4 T gas min/max = 433, 460.454 DICPCG: Solving for p, Initial residual = 0.961666, Final residual = 0.0911229, No Iterations 50 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00127057, global = 4.30145e-08, cumulative = 6.19897e-06 DICPCG: Solving for p, Initial residual = 0.782944, Final residual = 9.05438e-07, No Iterations 125 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.76904e-09, global = -8.86809e-14, cumulative = 6.19897e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0239926, Final residual = 1.22732e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0101853, Final residual = 5.50462e-06, No Iterations 3 Mean pressure:181605 Mean temperature:445.073 Mean u':0.328966 ExecutionTime = 2149.88 s ClockTime = 2236 s Courant Number mean: 0.0080484 max: 0.0539922 deltaT = 0.00100004 Crank angle = -89 CA-deg deltaZ = 0.000788812 clearance: 0.0649083 Piston speed = 0.78878 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.302762, Final residual = 1.4653e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.317183, Final residual = 9.82201e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.00778528, Final residual = 2.25399e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000205986, Final residual = 1.16032e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.259593, Final residual = 6.52734e-06, No Iterations 4 T gas min/max = 433, 462.248 DICPCG: Solving for p, Initial residual = 0.957903, Final residual = 0.0935859, No Iterations 47 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.0015974, global = 7.76348e-08, cumulative = 6.2766e-06 DICPCG: Solving for p, Initial residual = 0.800535, Final residual = 8.28555e-07, No Iterations 130 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.11524e-09, global = -7.44249e-14, cumulative = 6.2766e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0270492, Final residual = 2.69234e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0117115, Final residual = 1.09717e-06, No Iterations 4 Mean pressure:184624 Mean temperature:447.037 Mean u':0.327466 ExecutionTime = 2164.59 s ClockTime = 2251 s Courant Number mean: 0.00957996 max: 0.064545 deltaT = 0.000800032 Crank angle = -88.2 CA-deg deltaZ = 0.000635858 clearance: 0.0642725 Piston speed = 0.794791 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.241613, Final residual = 5.17284e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.255867, Final residual = 4.71514e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0178156, Final residual = 3.55251e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000171765, Final residual = 4.75421e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.216637, Final residual = 2.21764e-06, No Iterations 4 T gas min/max = 433, 463.715 DICPCG: Solving for p, Initial residual = 0.963741, Final residual = 0.0779513, No Iterations 50 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00107988, global = 2.62398e-08, cumulative = 6.30284e-06 DICPCG: Solving for p, Initial residual = 0.755959, Final residual = 9.10964e-07, No Iterations 126 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.59915e-09, global = -6.1615e-14, cumulative = 6.30284e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0217587, Final residual = 9.74715e-07, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.00916518, Final residual = 4.48164e-06, No Iterations 3 Mean pressure:187122 Mean temperature:448.646 Mean u':0.3263 ExecutionTime = 2179.28 s ClockTime = 2266 s Courant Number mean: 0.00800137 max: 0.0532443 deltaT = 0.000800032 Crank angle = -87.4 CA-deg deltaZ = 0.000639993 clearance: 0.0636325 Piston speed = 0.799959 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.206908, Final residual = 5.32623e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.206554, Final residual = 5.11063e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.00620178, Final residual = 7.87183e-07, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.00017438, Final residual = 3.93723e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.223386, Final residual = 2.30644e-06, No Iterations 4 T gas min/max = 433, 465.206 DICPCG: Solving for p, Initial residual = 0.963899, Final residual = 0.0789726, No Iterations 44 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00111204, global = 6.38703e-08, cumulative = 6.36671e-06 DICPCG: Solving for p, Initial residual = 0.770457, Final residual = 9.45771e-07, No Iterations 120 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.69643e-09, global = -1.92007e-14, cumulative = 6.36671e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0211299, Final residual = 9.88079e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00888939, Final residual = 4.37767e-06, No Iterations 3 Mean pressure:189697 Mean temperature:450.289 Mean u':0.32517 ExecutionTime = 2193.91 s ClockTime = 2280 s Courant Number mean: 0.00814237 max: 0.0537615 deltaT = 0.000800032 Crank angle = -86.6 CA-deg deltaZ = 0.000643993 clearance: 0.0629885 Piston speed = 0.80496 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.213738, Final residual = 4.4412e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.222076, Final residual = 4.12301e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.00658833, Final residual = 8.18923e-07, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000172855, Final residual = 3.93258e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.230078, Final residual = 2.39468e-06, No Iterations 4 T gas min/max = 433, 466.727 DICPCG: Solving for p, Initial residual = 0.965755, Final residual = 0.0899057, No Iterations 46 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00128397, global = 1.00121e-07, cumulative = 6.46683e-06 DICPCG: Solving for p, Initial residual = 0.796168, Final residual = 9.49455e-07, No Iterations 125 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.87125e-09, global = 4.68713e-14, cumulative = 6.46683e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0205078, Final residual = 9.65385e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00862142, Final residual = 4.27407e-06, No Iterations 3 Mean pressure:192350 Mean temperature:451.964 Mean u':0.324075 ExecutionTime = 2208.65 s ClockTime = 2295 s Courant Number mean: 0.00843023 max: 0.0558232 deltaT = 0.000800032 Crank angle = -85.8 CA-deg deltaZ = 0.000647857 clearance: 0.0623406 Piston speed = 0.809788 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.229953, Final residual = 5.30731e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.21311, Final residual = 6.5605e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.00939569, Final residual = 1.78823e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000173546, Final residual = 6.14065e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.23695, Final residual = 2.48843e-06, No Iterations 4 T gas min/max = 433, 468.287 DICPCG: Solving for p, Initial residual = 0.964375, Final residual = 0.0756029, No Iterations 49 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00109891, global = 4.10259e-08, cumulative = 6.50786e-06 DICPCG: Solving for p, Initial residual = 0.773119, Final residual = 9.23028e-07, No Iterations 123 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.65268e-09, global = 9.46981e-14, cumulative = 6.50786e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.019926, Final residual = 9.45013e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00834633, Final residual = 4.16104e-06, No Iterations 3 Mean pressure:195083 Mean temperature:453.671 Mean u':0.323015 ExecutionTime = 2223.42 s ClockTime = 2310 s Courant Number mean: 0.00829287 max: 0.0566178 deltaT = 0.000800032 Crank angle = -85 CA-deg deltaZ = 0.000651578 clearance: 0.0616891 Piston speed = 0.81444 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.223443, Final residual = 4.33161e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.235017, Final residual = 5.11566e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0105111, Final residual = 1.95229e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000176637, Final residual = 5.2689e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.244077, Final residual = 2.5826e-06, No Iterations 4 T gas min/max = 433, 469.871 DICPCG: Solving for p, Initial residual = 0.966072, Final residual = 0.0709128, No Iterations 49 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.0010449, global = 4.20827e-08, cumulative = 6.54994e-06 DICPCG: Solving for p, Initial residual = 0.757128, Final residual = 8.11243e-07, No Iterations 123 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.40377e-09, global = 3.52706e-14, cumulative = 6.54994e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0193266, Final residual = 9.26615e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00807553, Final residual = 4.06614e-06, No Iterations 3 Mean pressure:197900 Mean temperature:455.41 Mean u':0.321991 ExecutionTime = 2239.65 s ClockTime = 2327 s Courant Number mean: 0.00874091 max: 0.0575699 deltaT = 0.000833367 Crank angle = -84.1667 CA-deg deltaZ = 0.000682528 clearance: 0.0610065 Piston speed = 0.819 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.255151, Final residual = 5.93147e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.237929, Final residual = 5.84107e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.00611748, Final residual = 1.39332e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000177878, Final residual = 8.02026e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.261397, Final residual = 3.32447e-06, No Iterations 4 T gas min/max = 433, 471.545 DICPCG: Solving for p, Initial residual = 0.966599, Final residual = 0.0822262, No Iterations 48 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00128096, global = 7.04543e-08, cumulative = 6.6204e-06 DICPCG: Solving for p, Initial residual = 0.782834, Final residual = 7.72167e-07, No Iterations 123 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.5424e-09, global = -7.95166e-14, cumulative = 6.6204e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0193904, Final residual = 1.05628e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.00810417, Final residual = 4.61177e-06, No Iterations 3 Mean pressure:200926 Mean temperature:457.256 Mean u':0.320963 ExecutionTime = 2254.42 s ClockTime = 2342 s Courant Number mean: 0.0090292 max: 0.0618999 deltaT = 0.000833367 Crank angle = -83.3333 CA-deg deltaZ = 0.000686239 clearance: 0.0603203 Piston speed = 0.823454 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.291886, Final residual = 6.65226e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.328015, Final residual = 7.43095e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0138228, Final residual = 3.09272e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000179974, Final residual = 6.09857e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.269598, Final residual = 3.46014e-06, No Iterations 4 T gas min/max = 433, 473.244 DICPCG: Solving for p, Initial residual = 0.965456, Final residual = 0.0933972, No Iterations 49 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00148043, global = 6.41407e-08, cumulative = 6.68454e-06 DICPCG: Solving for p, Initial residual = 0.807277, Final residual = 9.24013e-07, No Iterations 123 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.06671e-09, global = 8.42482e-14, cumulative = 6.68454e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0187507, Final residual = 1.03791e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.007809, Final residual = 4.4939e-06, No Iterations 3 Mean pressure:204048 Mean temperature:459.136 Mean u':0.319974 ExecutionTime = 2269.19 s ClockTime = 2357 s Courant Number mean: 0.0094259 max: 0.0612735 deltaT = 0.000833367 Crank angle = -82.5 CA-deg deltaZ = 0.000689777 clearance: 0.0596305 Piston speed = 0.827699 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.315334, Final residual = 7.17558e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.304635, Final residual = 7.07915e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.00785257, Final residual = 1.55998e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000178513, Final residual = 5.45174e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.27823, Final residual = 3.63101e-06, No Iterations 4 T gas min/max = 433, 475.019 DICPCG: Solving for p, Initial residual = 0.964843, Final residual = 0.094295, No Iterations 49 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00151978, global = 1.06994e-07, cumulative = 6.79153e-06 DICPCG: Solving for p, Initial residual = 0.812138, Final residual = 8.09922e-07, No Iterations 124 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.86966e-09, global = 5.3256e-14, cumulative = 6.79153e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0181034, Final residual = 1.01193e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.00751916, Final residual = 4.35844e-06, No Iterations 3 Mean pressure:207271 Mean temperature:461.054 Mean u':0.319021 ExecutionTime = 2283.84 s ClockTime = 2372 s Courant Number mean: 0.00974031 max: 0.0655256 deltaT = 0.000833367 Crank angle = -81.6667 CA-deg deltaZ = 0.000693137 clearance: 0.0589374 Piston speed = 0.831731 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.341959, Final residual = 7.41947e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.371394, Final residual = 8.2066e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.00706746, Final residual = 1.28966e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000176764, Final residual = 5.21031e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.287208, Final residual = 3.78256e-06, No Iterations 4 T gas min/max = 433, 476.838 DICPCG: Solving for p, Initial residual = 0.964554, Final residual = 0.0915617, No Iterations 53 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00150016, global = 3.39982e-08, cumulative = 6.82553e-06 DICPCG: Solving for p, Initial residual = 0.815415, Final residual = 8.23747e-07, No Iterations 116 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.91483e-09, global = 2.01892e-14, cumulative = 6.82553e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.017475, Final residual = 9.83366e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00722681, Final residual = 4.24019e-06, No Iterations 3 Mean pressure:210599 Mean temperature:463.009 Mean u':0.318106 ExecutionTime = 2298.52 s ClockTime = 2386 s Courant Number mean: 0.00994731 max: 0.064922 deltaT = 0.000833367 Crank angle = -80.8333 CA-deg deltaZ = 0.000696315 clearance: 0.0582411 Piston speed = 0.835545 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.262726, Final residual = 6.19883e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.259616, Final residual = 7.27471e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.00731088, Final residual = 1.48389e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000177297, Final residual = 8.57958e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.296489, Final residual = 3.97464e-06, No Iterations 4 T gas min/max = 433, 478.685 DICPCG: Solving for p, Initial residual = 0.964938, Final residual = 0.0912866, No Iterations 49 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00151873, global = 8.53607e-08, cumulative = 6.91089e-06 DICPCG: Solving for p, Initial residual = 0.816483, Final residual = 8.32017e-07, No Iterations 123 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.88634e-09, global = 1.43564e-14, cumulative = 6.91089e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0168407, Final residual = 9.56599e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00693708, Final residual = 4.10977e-06, No Iterations 3 Mean pressure:214035 Mean temperature:465.002 Mean u':0.317228 ExecutionTime = 2313.22 s ClockTime = 2401 s Courant Number mean: 0.0102189 max: 0.0686977 deltaT = 0.000833367 Crank angle = -80 CA-deg deltaZ = 0.000699307 clearance: 0.0575418 Piston speed = 0.839135 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.31107, Final residual = 7.196e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.323662, Final residual = 7.45613e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.00593866, Final residual = 1.1836e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000179503, Final residual = 1.49572e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.306001, Final residual = 4.14762e-06, No Iterations 4 T gas min/max = 433, 480.575 DICPCG: Solving for p, Initial residual = 0.966133, Final residual = 0.0860478, No Iterations 50 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00145265, global = 8.09054e-08, cumulative = 6.9918e-06 DICPCG: Solving for p, Initial residual = 0.806776, Final residual = 9.89159e-07, No Iterations 125 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.21192e-09, global = -5.48065e-14, cumulative = 6.9918e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0162143, Final residual = 9.35513e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00664609, Final residual = 3.98507e-06, No Iterations 3 Mean pressure:217583 Mean temperature:467.035 Mean u':0.316387 ExecutionTime = 2329.67 s ClockTime = 2423 s Courant Number mean: 0.0106285 max: 0.0672971 deltaT = 0.00100004 Crank angle = -79 CA-deg deltaZ = 0.00084285 clearance: 0.0566989 Piston speed = 0.842816 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.39978, Final residual = 2.5224e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.391834, Final residual = 2.1963e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.00866217, Final residual = 3.50662e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000200612, Final residual = 2.90688e-07, No Iterations 3 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.369823, Final residual = 1.01352e-06, No Iterations 5 T gas min/max = 433, 482.883 DICPCG: Solving for p, Initial residual = 0.963264, Final residual = 0.089984, No Iterations 55 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00185478, global = 2.9145e-08, cumulative = 7.02094e-06 DICPCG: Solving for p, Initial residual = 0.817479, Final residual = 9.69397e-07, No Iterations 124 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.79225e-09, global = 4.1256e-15, cumulative = 7.02094e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0180253, Final residual = 2.0496e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.00751832, Final residual = 7.46445e-06, No Iterations 3 Mean pressure:221991 Mean temperature:469.514 Mean u':0.315431 ExecutionTime = 2344.5 s ClockTime = 2438 s Courant Number mean: 0.0126827 max: 0.0855733 deltaT = 0.000800032 Crank angle = -78.2 CA-deg deltaZ = 0.000676959 clearance: 0.0560219 Piston speed = 0.846165 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.209769, Final residual = 5.10624e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.252886, Final residual = 4.50177e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.00786, Final residual = 1.51128e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.00017531, Final residual = 5.34409e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.315034, Final residual = 3.7357e-06, No Iterations 4 T gas min/max = 433, 484.77 DICPCG: Solving for p, Initial residual = 0.970314, Final residual = 0.0928108, No Iterations 49 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00154962, global = 8.99017e-08, cumulative = 7.11084e-06 DICPCG: Solving for p, Initial residual = 0.820828, Final residual = 7.97316e-07, No Iterations 123 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.80055e-09, global = 2.92961e-14, cumulative = 7.11084e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0143482, Final residual = 7.59886e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00578974, Final residual = 3.18277e-06, No Iterations 3 Mean pressure:225646 Mean temperature:471.547 Mean u':0.314699 ExecutionTime = 2359.32 s ClockTime = 2452 s Courant Number mean: 0.01053 max: 0.0684669 deltaT = 0.000800032 Crank angle = -77.4 CA-deg deltaZ = 0.00067915 clearance: 0.0553428 Piston speed = 0.848904 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.30722, Final residual = 5.78472e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.311434, Final residual = 6.07376e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.00555357, Final residual = 7.5984e-07, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000178553, Final residual = 8.09988e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.324548, Final residual = 3.92127e-06, No Iterations 4 T gas min/max = 433, 486.687 DICPCG: Solving for p, Initial residual = 0.967953, Final residual = 0.0911913, No Iterations 49 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00154998, global = 6.39035e-08, cumulative = 7.17475e-06 DICPCG: Solving for p, Initial residual = 0.830021, Final residual = 9.11025e-07, No Iterations 122 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.075e-09, global = -6.8661e-14, cumulative = 7.17475e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0137554, Final residual = 7.37586e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00552461, Final residual = 3.06551e-06, No Iterations 3 Mean pressure:229421 Mean temperature:473.622 Mean u':0.314001 ExecutionTime = 2374.08 s ClockTime = 2467 s Courant Number mean: 0.0106021 max: 0.0716821 deltaT = 0.000800032 Crank angle = -76.6 CA-deg deltaZ = 0.000681162 clearance: 0.0546616 Piston speed = 0.851419 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.28147, Final residual = 6.89369e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.297745, Final residual = 5.9594e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.00803224, Final residual = 1.80983e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000175582, Final residual = 4.77766e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.333342, Final residual = 4.09419e-06, No Iterations 4 T gas min/max = 433, 488.635 DICPCG: Solving for p, Initial residual = 0.968802, Final residual = 0.0923207, No Iterations 51 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00159152, global = 5.46833e-08, cumulative = 7.22943e-06 DICPCG: Solving for p, Initial residual = 0.834806, Final residual = 9.87116e-07, No Iterations 123 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.24797e-09, global = 4.51555e-14, cumulative = 7.22943e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.013166, Final residual = 7.17742e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00526352, Final residual = 2.9716e-06, No Iterations 3 Mean pressure:233317 Mean temperature:475.736 Mean u':0.313335 ExecutionTime = 2388.86 s ClockTime = 2482 s Courant Number mean: 0.0109623 max: 0.0716132 deltaT = 0.000800032 Crank angle = -75.8 CA-deg deltaZ = 0.000682992 clearance: 0.0539786 Piston speed = 0.853706 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.287344, Final residual = 5.12971e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.263907, Final residual = 4.756e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.00624424, Final residual = 9.07225e-07, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000179899, Final residual = 7.80285e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.341634, Final residual = 4.28355e-06, No Iterations 4 T gas min/max = 433, 490.611 DICPCG: Solving for p, Initial residual = 0.968535, Final residual = 0.0900865, No Iterations 49 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00157639, global = 9.72606e-08, cumulative = 7.32669e-06 DICPCG: Solving for p, Initial residual = 0.84019, Final residual = 9.84512e-07, No Iterations 128 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.22525e-09, global = -1.62438e-14, cumulative = 7.32669e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0125772, Final residual = 6.94273e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00500056, Final residual = 2.85679e-06, No Iterations 3 Mean pressure:237340 Mean temperature:477.89 Mean u':0.312703 ExecutionTime = 2403.63 s ClockTime = 2497 s Courant Number mean: 0.0110508 max: 0.0752716 deltaT = 0.000800032 Crank angle = -75 CA-deg deltaZ = 0.000684637 clearance: 0.053294 Piston speed = 0.855762 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.293789, Final residual = 6.14871e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.315551, Final residual = 5.99318e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.00881143, Final residual = 2.0548e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000182056, Final residual = 9.36522e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.34957, Final residual = 4.44884e-06, No Iterations 4 T gas min/max = 433, 492.642 DICPCG: Solving for p, Initial residual = 0.969481, Final residual = 0.090058, No Iterations 52 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00159757, global = 6.36191e-08, cumulative = 7.39031e-06 DICPCG: Solving for p, Initial residual = 0.843271, Final residual = 7.59761e-07, No Iterations 124 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.79335e-09, global = 3.79603e-14, cumulative = 7.39031e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0119848, Final residual = 6.73386e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00474069, Final residual = 2.75402e-06, No Iterations 3 Mean pressure:241493 Mean temperature:480.085 Mean u':0.312103 ExecutionTime = 2420.1 s ClockTime = 2518 s Courant Number mean: 0.0113494 max: 0.0736532 deltaT = 0.000833367 Crank angle = -74.1667 CA-deg deltaZ = 0.00071471 clearance: 0.0525793 Piston speed = 0.857618 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.283236, Final residual = 7.51435e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.258541, Final residual = 6.08907e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.00932695, Final residual = 2.57914e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000183821, Final residual = 2.3979e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.369379, Final residual = 5.69587e-06, No Iterations 4 T gas min/max = 433, 494.803 DICPCG: Solving for p, Initial residual = 0.969125, Final residual = 0.0966268, No Iterations 50 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00181183, global = 1.15185e-07, cumulative = 7.50549e-06 DICPCG: Solving for p, Initial residual = 0.860741, Final residual = 8.328e-07, No Iterations 127 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.14757e-09, global = -9.75871e-14, cumulative = 7.50549e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0117718, Final residual = 7.51908e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00465072, Final residual = 3.04962e-06, No Iterations 3 Mean pressure:245962 Mean temperature:482.411 Mean u':0.311513 ExecutionTime = 2434.8 s ClockTime = 2533 s Courant Number mean: 0.0121149 max: 0.0807755 deltaT = 0.000833367 Crank angle = -73.3333 CA-deg deltaZ = 0.000716076 clearance: 0.0518632 Piston speed = 0.859257 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.326355, Final residual = 7.7379e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.332994, Final residual = 7.61349e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0091014, Final residual = 2.20379e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000180355, Final residual = 9.78587e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.376666, Final residual = 5.93298e-06, No Iterations 4 T gas min/max = 433, 497.027 DICPCG: Solving for p, Initial residual = 0.967264, Final residual = 0.0715248, No Iterations 54 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00136394, global = 3.75282e-08, cumulative = 7.54302e-06 DICPCG: Solving for p, Initial residual = 0.831338, Final residual = 9.11308e-07, No Iterations 125 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.01453e-09, global = 3.64841e-14, cumulative = 7.54302e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0111308, Final residual = 7.2373e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0043732, Final residual = 2.93235e-06, No Iterations 3 Mean pressure:250584 Mean temperature:484.782 Mean u':0.310958 ExecutionTime = 2449.7 s ClockTime = 2548 s Courant Number mean: 0.0122 max: 0.0797391 deltaT = 0.000833367 Crank angle = -72.5 CA-deg deltaZ = 0.000717223 clearance: 0.051146 Piston speed = 0.860633 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.165942, Final residual = 4.6214e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.170256, Final residual = 4.46019e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0079862, Final residual = 2.20873e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000184511, Final residual = 1.18683e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.383657, Final residual = 6.18507e-06, No Iterations 4 T gas min/max = 433, 499.297 DICPCG: Solving for p, Initial residual = 0.973117, Final residual = 0.0970384, No Iterations 47 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00186696, global = 8.89553e-08, cumulative = 7.63198e-06 DICPCG: Solving for p, Initial residual = 0.862478, Final residual = 9.97868e-07, No Iterations 123 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.58894e-09, global = 2.36219e-13, cumulative = 7.63198e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0104879, Final residual = 6.92711e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00409597, Final residual = 2.78396e-06, No Iterations 3 Mean pressure:255364 Mean temperature:487.198 Mean u':0.310438 ExecutionTime = 2464.41 s ClockTime = 2563 s Courant Number mean: 0.0127046 max: 0.0836 deltaT = 0.000833367 Crank angle = -71.6667 CA-deg deltaZ = 0.000718148 clearance: 0.0504278 Piston speed = 0.861743 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.283453, Final residual = 7.90792e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.30291, Final residual = 5.95812e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.00730113, Final residual = 1.72178e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000185801, Final residual = 1.41246e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.390382, Final residual = 6.44168e-06, No Iterations 4 T gas min/max = 433, 501.602 DICPCG: Solving for p, Initial residual = 0.969876, Final residual = 0.0818986, No Iterations 49 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00160445, global = 6.42166e-08, cumulative = 7.69619e-06 DICPCG: Solving for p, Initial residual = 0.846023, Final residual = 9.69018e-07, No Iterations 127 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.27679e-09, global = -4.81709e-14, cumulative = 7.69619e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.009856, Final residual = 6.61623e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00382408, Final residual = 2.64211e-06, No Iterations 3 Mean pressure:260310 Mean temperature:489.661 Mean u':0.309951 ExecutionTime = 2479.16 s ClockTime = 2578 s Courant Number mean: 0.0126654 max: 0.0834821 deltaT = 0.000833367 Crank angle = -70.8333 CA-deg deltaZ = 0.000718849 clearance: 0.049709 Piston speed = 0.862585 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.213206, Final residual = 7.491e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.215418, Final residual = 6.82066e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.00635881, Final residual = 1.88169e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000187123, Final residual = 4.66042e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.396852, Final residual = 6.7015e-06, No Iterations 4 T gas min/max = 433, 503.943 DICPCG: Solving for p, Initial residual = 0.97251, Final residual = 0.0963729, No Iterations 48 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00191083, global = 7.04438e-08, cumulative = 7.76664e-06 DICPCG: Solving for p, Initial residual = 0.85487, Final residual = 8.41976e-07, No Iterations 125 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.24634e-09, global = 5.12981e-14, cumulative = 7.76664e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.00922007, Final residual = 6.33061e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00354998, Final residual = 2.48969e-06, No Iterations 3 Mean pressure:265429 Mean temperature:492.17 Mean u':0.309499 ExecutionTime = 2493.83 s ClockTime = 2592 s Courant Number mean: 0.013165 max: 0.0858324 deltaT = 0.000833367 Crank angle = -70 CA-deg deltaZ = 0.000719324 clearance: 0.0489897 Piston speed = 0.863154 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.297986, Final residual = 9.18397e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.303907, Final residual = 6.535e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0076056, Final residual = 2.22735e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000186302, Final residual = 7.3417e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.40311, Final residual = 6.98201e-06, No Iterations 4 T gas min/max = 433, 506.32 DICPCG: Solving for p, Initial residual = 0.969805, Final residual = 0.0944127, No Iterations 53 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00190488, global = 3.88981e-08, cumulative = 7.80554e-06 DICPCG: Solving for p, Initial residual = 0.871426, Final residual = 9.00746e-07, No Iterations 126 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.4802e-09, global = 5.27232e-14, cumulative = 7.80554e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.00860649, Final residual = 6.08999e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00328168, Final residual = 2.3617e-06, No Iterations 3 Mean pressure:270726 Mean temperature:494.728 Mean u':0.30908 ExecutionTime = 2510.32 s ClockTime = 2615 s Courant Number mean: 0.0132672 max: 0.0863236 deltaT = 0.00100004 Crank angle = -69 CA-deg deltaZ = 0.000863491 clearance: 0.0481262 Piston speed = 0.863456 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.204372, Final residual = 1.42225e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.224146, Final residual = 1.571e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.00812769, Final residual = 4.07704e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000208066, Final residual = 2.04774e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.466071, Final residual = 1.53765e-06, No Iterations 5 T gas min/max = 433, 509.201 DICPCG: Solving for p, Initial residual = 0.9692, Final residual = 0.0828913, No Iterations 50 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00203362, global = 1.0947e-07, cumulative = 7.91501e-06 DICPCG: Solving for p, Initial residual = 0.854039, Final residual = 8.36362e-07, No Iterations 130 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.52988e-09, global = 7.95706e-15, cumulative = 7.91501e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.00928754, Final residual = 1.36278e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0035375, Final residual = 4.13686e-06, No Iterations 3 Mean pressure:277320 Mean temperature:497.845 Mean u':0.308625 ExecutionTime = 2525.11 s ClockTime = 2629 s Courant Number mean: 0.0162834 max: 0.108247 deltaT = 0.000800032 Crank angle = -68.2 CA-deg deltaZ = 0.000690777 clearance: 0.0474354 Piston speed = 0.863437 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.291462, Final residual = 6.16181e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.294244, Final residual = 6.18548e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.00863995, Final residual = 2.33766e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000179911, Final residual = 8.39925e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.403065, Final residual = 6.22298e-06, No Iterations 4 T gas min/max = 433, 511.577 DICPCG: Solving for p, Initial residual = 0.974199, Final residual = 0.0740926, No Iterations 53 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00147462, global = 3.83914e-08, cumulative = 7.9534e-06 DICPCG: Solving for p, Initial residual = 0.846081, Final residual = 9.6157e-07, No Iterations 126 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.11426e-09, global = 7.3753e-14, cumulative = 7.9534e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.00721055, Final residual = 4.85605e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00260627, Final residual = 1.72618e-06, No Iterations 3 Mean pressure:282803 Mean temperature:500.401 Mean u':0.308292 ExecutionTime = 2539.85 s ClockTime = 2644 s Courant Number mean: 0.0132954 max: 0.0865103 deltaT = 0.000800032 Crank angle = -67.4 CA-deg deltaZ = 0.000690539 clearance: 0.0467449 Piston speed = 0.863139 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.19567, Final residual = 5.37587e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.174808, Final residual = 3.82453e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.00759481, Final residual = 2.1491e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000183448, Final residual = 5.53663e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.409124, Final residual = 6.50286e-06, No Iterations 4 T gas min/max = 433, 513.999 DICPCG: Solving for p, Initial residual = 0.974502, Final residual = 0.084822, No Iterations 48 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00171173, global = 1.01739e-07, cumulative = 8.05514e-06 DICPCG: Solving for p, Initial residual = 0.855448, Final residual = 8.09734e-07, No Iterations 125 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.93935e-09, global = 2.79954e-14, cumulative = 8.05514e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.00679562, Final residual = 4.69135e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00236387, Final residual = 1.59783e-06, No Iterations 3 Mean pressure:288476 Mean temperature:503.009 Mean u':0.30799 ExecutionTime = 2554.53 s ClockTime = 2659 s Courant Number mean: 0.0137221 max: 0.0889479 deltaT = 0.000800032 Crank angle = -66.6 CA-deg deltaZ = 0.000690092 clearance: 0.0460548 Piston speed = 0.862581 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.300982, Final residual = 7.34757e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.311298, Final residual = 6.54877e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.00751595, Final residual = 1.59875e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000182308, Final residual = 7.38423e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.414549, Final residual = 6.7457e-06, No Iterations 4 T gas min/max = 433, 516.459 DICPCG: Solving for p, Initial residual = 0.973205, Final residual = 0.0911139, No Iterations 50 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00186664, global = 1.28025e-07, cumulative = 8.18316e-06 DICPCG: Solving for p, Initial residual = 0.88579, Final residual = 7.61551e-07, No Iterations 127 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.04073e-09, global = -4.57523e-14, cumulative = 8.18316e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.00641156, Final residual = 4.52695e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0021327, Final residual = 1.44411e-06, No Iterations 3 Mean pressure:294345 Mean temperature:505.665 Mean u':0.307718 ExecutionTime = 2569.21 s ClockTime = 2674 s Courant Number mean: 0.0141781 max: 0.089392 deltaT = 0.000800032 Crank angle = -65.8 CA-deg deltaZ = 0.000689435 clearance: 0.0453653 Piston speed = 0.861759 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.293268, Final residual = 9.76656e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.212756, Final residual = 5.39909e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0166552, Final residual = 4.69225e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000182334, Final residual = 8.80476e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.41957, Final residual = 7.04108e-06, No Iterations 4 T gas min/max = 433, 518.956 DICPCG: Solving for p, Initial residual = 0.97141, Final residual = 0.0920778, No Iterations 53 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00191697, global = 5.55418e-08, cumulative = 8.2387e-06 DICPCG: Solving for p, Initial residual = 0.884587, Final residual = 9.87354e-07, No Iterations 124 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.74632e-09, global = 1.03474e-13, cumulative = 8.2387e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.00606688, Final residual = 4.35496e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00190947, Final residual = 1.29766e-06, No Iterations 3 Mean pressure:300416 Mean temperature:508.369 Mean u':0.307476 ExecutionTime = 2583.99 s ClockTime = 2688 s Courant Number mean: 0.0143763 max: 0.0922106 deltaT = 0.000800032 Crank angle = -65 CA-deg deltaZ = 0.000688565 clearance: 0.0446768 Piston speed = 0.860672 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.245751, Final residual = 5.62055e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.220105, Final residual = 7.91015e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.00936194, Final residual = 2.81939e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000185526, Final residual = 7.44797e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.424192, Final residual = 7.29126e-06, No Iterations 4 T gas min/max = 433, 521.536 DICPCG: Solving for p, Initial residual = 0.972434, Final residual = 0.0926965, No Iterations 53 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.0019529, global = 8.53778e-08, cumulative = 8.32408e-06 DICPCG: Solving for p, Initial residual = 0.907245, Final residual = 8.13474e-07, No Iterations 126 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.32444e-09, global = 4.694e-14, cumulative = 8.32408e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.00574874, Final residual = 4.20559e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00170491, Final residual = 1.20744e-06, No Iterations 3 Mean pressure:306698 Mean temperature:511.122 Mean u':0.307263 ExecutionTime = 2600.34 s ClockTime = 2707 s Courant Number mean: 0.0147242 max: 0.0920441 deltaT = 0.000833367 Crank angle = -64.1667 CA-deg deltaZ = 0.000716101 clearance: 0.0439607 Piston speed = 0.859287 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.245785, Final residual = 9.66932e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.187718, Final residual = 6.97741e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0102182, Final residual = 3.58998e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000189914, Final residual = 7.98591e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.43981, Final residual = 9.20639e-06, No Iterations 4 T gas min/max = 433, 524.258 DICPCG: Solving for p, Initial residual = 0.973876, Final residual = 0.0932191, No Iterations 53 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00206876, global = 9.79892e-08, cumulative = 8.42207e-06 DICPCG: Solving for p, Initial residual = 0.900859, Final residual = 9.34175e-07, No Iterations 125 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.77695e-09, global = -1.86874e-14, cumulative = 8.42207e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.00563926, Final residual = 4.6728e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00156105, Final residual = 1.412e-06, No Iterations 3 Mean pressure:313473 Mean temperature:514.04 Mean u':0.307073 ExecutionTime = 2615.12 s ClockTime = 2721 s Courant Number mean: 0.0158077 max: 0.0991389 deltaT = 0.000833367 Crank angle = -63.3333 CA-deg deltaZ = 0.000714684 clearance: 0.043246 Piston speed = 0.857587 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.217611, Final residual = 7.70832e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.232265, Final residual = 7.06567e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0112658, Final residual = 4.33253e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000189201, Final residual = 9.05364e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.443378, Final residual = 9.52993e-06, No Iterations 4 T gas min/max = 433, 527.021 DICPCG: Solving for p, Initial residual = 0.973544, Final residual = 0.0960009, No Iterations 53 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.0021605, global = 1.09854e-07, cumulative = 8.53193e-06 DICPCG: Solving for p, Initial residual = 0.901288, Final residual = 7.82994e-07, No Iterations 126 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.38222e-09, global = 1.03254e-13, cumulative = 8.53193e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.00533827, Final residual = 4.46198e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00137983, Final residual = 1.94275e-06, No Iterations 3 Mean pressure:320495 Mean temperature:517.011 Mean u':0.306914 ExecutionTime = 2629.91 s ClockTime = 2736 s Courant Number mean: 0.0161829 max: 0.098934 deltaT = 0.000833367 Crank angle = -62.5 CA-deg deltaZ = 0.000713024 clearance: 0.042533 Piston speed = 0.855595 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.255314, Final residual = 8.3715e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.204274, Final residual = 6.84518e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0117439, Final residual = 4.14086e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000190676, Final residual = 9.4464e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.446575, Final residual = 9.90323e-06, No Iterations 4 T gas min/max = 433, 529.824 DICPCG: Solving for p, Initial residual = 0.973318, Final residual = 0.0923098, No Iterations 53 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00210635, global = 1.1697e-07, cumulative = 8.6489e-06 DICPCG: Solving for p, Initial residual = 0.892958, Final residual = 8.86468e-07, No Iterations 122 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.6577e-09, global = -1.06762e-14, cumulative = 8.6489e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.00505179, Final residual = 4.21494e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00122348, Final residual = 6.97883e-06, No Iterations 3 Mean pressure:327775 Mean temperature:520.037 Mean u':0.306786 ExecutionTime = 2644.65 s ClockTime = 2751 s Courant Number mean: 0.0167521 max: 0.10415 deltaT = 0.000833367 Crank angle = -61.6667 CA-deg deltaZ = 0.000711119 clearance: 0.0418218 Piston speed = 0.853309 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.225318, Final residual = 8.93793e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.249786, Final residual = 7.32868e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0125395, Final residual = 4.90352e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000191772, Final residual = 5.26933e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.449174, Final residual = 7.61108e-07, No Iterations 5 T gas min/max = 433, 532.67 DICPCG: Solving for p, Initial residual = 0.973005, Final residual = 0.0848838, No Iterations 54 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00196386, global = 8.21803e-08, cumulative = 8.73108e-06 DICPCG: Solving for p, Initial residual = 0.886891, Final residual = 7.86811e-07, No Iterations 126 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.2322e-09, global = 1.04756e-14, cumulative = 8.73108e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.00477915, Final residual = 3.96143e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00111034, Final residual = 4.37583e-06, No Iterations 3 Mean pressure:335323 Mean temperature:523.118 Mean u':0.306687 ExecutionTime = 2659.46 s ClockTime = 2766 s Courant Number mean: 0.0170479 max: 0.103151 deltaT = 0.000833367 Crank angle = -60.8333 CA-deg deltaZ = 0.00070897 clearance: 0.0411129 Piston speed = 0.850729 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.208952, Final residual = 6.24079e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.186923, Final residual = 6.98057e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.01122, Final residual = 4.12164e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000191669, Final residual = 1.04422e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.451045, Final residual = 7.85059e-07, No Iterations 5 T gas min/max = 433, 535.585 DICPCG: Solving for p, Initial residual = 0.975437, Final residual = 0.0915898, No Iterations 51 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00214214, global = 1.14605e-07, cumulative = 8.84568e-06 DICPCG: Solving for p, Initial residual = 0.886699, Final residual = 7.48203e-07, No Iterations 124 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.21082e-09, global = -2.61699e-14, cumulative = 8.84568e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.00452079, Final residual = 3.6996e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00103548, Final residual = 1.77876e-06, No Iterations 3 Mean pressure:343152 Mean temperature:526.257 Mean u':0.306619 ExecutionTime = 2674.27 s ClockTime = 2781 s Courant Number mean: 0.017677 max: 0.107021 deltaT = 0.000833367 Crank angle = -60 CA-deg deltaZ = 0.000706574 clearance: 0.0404063 Piston speed = 0.847855 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.221287, Final residual = 6.78357e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.285677, Final residual = 9.49846e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0115437, Final residual = 4.43781e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000191285, Final residual = 2.86625e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.451994, Final residual = 8.05705e-07, No Iterations 5 T gas min/max = 433, 538.548 DICPCG: Solving for p, Initial residual = 0.973787, Final residual = 0.0837834, No Iterations 54 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00198906, global = 9.37139e-08, cumulative = 8.93939e-06 DICPCG: Solving for p, Initial residual = 0.883734, Final residual = 9.70935e-07, No Iterations 125 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.78227e-09, global = -8.33509e-14, cumulative = 8.93939e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.00430483, Final residual = 3.39592e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0010014, Final residual = 8.24456e-07, No Iterations 3 Mean pressure:351273 Mean temperature:529.453 Mean u':0.306578 ExecutionTime = 2690.68 s ClockTime = 2800 s Courant Number mean: 0.0181071 max: 0.106491 deltaT = 0.00100004 Crank angle = -59 CA-deg deltaZ = 0.000844379 clearance: 0.0395619 Piston speed = 0.844345 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.238149, Final residual = 2.47506e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.219079, Final residual = 2.26737e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0203181, Final residual = 1.21143e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000219983, Final residual = 2.25107e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.498556, Final residual = 2.18409e-06, No Iterations 5 T gas min/max = 433, 542.135 DICPCG: Solving for p, Initial residual = 0.97261, Final residual = 0.0767725, No Iterations 52 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00221309, global = 7.62945e-08, cumulative = 9.01569e-06 DICPCG: Solving for p, Initial residual = 0.867235, Final residual = 9.8748e-07, No Iterations 128 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.30697e-09, global = 9.48835e-14, cumulative = 9.01569e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.00487107, Final residual = 5.83689e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00113225, Final residual = 1.60822e-06, No Iterations 3 Mean pressure:361405 Mean temperature:533.343 Mean u':0.306567 ExecutionTime = 2705.54 s ClockTime = 2815 s Courant Number mean: 0.0218444 max: 0.130576 deltaT = 0.00100004 Crank angle = -58 CA-deg deltaZ = 0.000840148 clearance: 0.0387218 Piston speed = 0.840114 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.188301, Final residual = 1.46113e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.196845, Final residual = 2.26103e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0141446, Final residual = 9.93962e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.00021638, Final residual = 1.74908e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.499005, Final residual = 2.2484e-06, No Iterations 5 T gas min/max = 433, 545.931 DICPCG: Solving for p, Initial residual = 0.975606, Final residual = 0.0950772, No Iterations 50 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00277465, global = 1.20573e-07, cumulative = 9.13626e-06 DICPCG: Solving for p, Initial residual = 0.890174, Final residual = 7.46104e-07, No Iterations 128 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.99526e-09, global = 9.10062e-14, cumulative = 9.13626e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.0047382, Final residual = 5.43332e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00110516, Final residual = 1.08418e-06, No Iterations 3 Mean pressure:371993 Mean temperature:537.311 Mean u':0.306594 ExecutionTime = 2720.29 s ClockTime = 2829 s Courant Number mean: 0.0215871 max: 0.128998 deltaT = 0.00100004 Crank angle = -57 CA-deg deltaZ = 0.00083549 clearance: 0.0378863 Piston speed = 0.835457 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.297001, Final residual = 3.63029e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.246356, Final residual = 2.41193e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0174947, Final residual = 1.24097e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000216386, Final residual = 1.81985e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.499048, Final residual = 2.32705e-06, No Iterations 5 T gas min/max = 433, 549.988 DICPCG: Solving for p, Initial residual = 0.971356, Final residual = 0.0906097, No Iterations 54 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00269681, global = 1.04871e-07, cumulative = 9.24113e-06 DICPCG: Solving for p, Initial residual = 0.879036, Final residual = 8.31581e-07, No Iterations 128 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.41215e-09, global = -1.26752e-14, cumulative = 9.24113e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.00465356, Final residual = 4.84562e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0011977, Final residual = 4.46515e-06, No Iterations 3 Mean pressure:383062 Mean temperature:541.363 Mean u':0.306656 ExecutionTime = 2735.15 s ClockTime = 2844 s Courant Number mean: 0.022219 max: 0.135489 deltaT = 0.00100004 Crank angle = -56 CA-deg deltaZ = 0.000830405 clearance: 0.0370559 Piston speed = 0.830372 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.331927, Final residual = 2.71067e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.210282, Final residual = 1.74459e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0230277, Final residual = 1.65023e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000218397, Final residual = 8.12952e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.498183, Final residual = 2.40645e-06, No Iterations 5 T gas min/max = 433, 554.125 DICPCG: Solving for p, Initial residual = 0.970749, Final residual = 0.0848178, No Iterations 57 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00256317, global = 4.43294e-08, cumulative = 9.28546e-06 DICPCG: Solving for p, Initial residual = 0.860512, Final residual = 8.36066e-07, No Iterations 128 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.16475e-09, global = -2.37995e-14, cumulative = 9.28546e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.00460288, Final residual = 4.15636e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00129775, Final residual = 7.94425e-06, No Iterations 2 Mean pressure:394640 Mean temperature:545.502 Mean u':0.306751 ExecutionTime = 2749.93 s ClockTime = 2859 s Courant Number mean: 0.0219223 max: 0.13291 deltaT = 0.00100004 Crank angle = -55 CA-deg deltaZ = 0.000824895 clearance: 0.036231 Piston speed = 0.824862 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.227387, Final residual = 1.51472e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.235335, Final residual = 2.42524e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0102525, Final residual = 5.72468e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000213363, Final residual = 1.45974e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.496581, Final residual = 2.48405e-06, No Iterations 5 T gas min/max = 433, 558.355 DICPCG: Solving for p, Initial residual = 0.973107, Final residual = 0.0949927, No Iterations 56 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00290655, global = 9.53542e-08, cumulative = 9.38082e-06 DICPCG: Solving for p, Initial residual = 0.884185, Final residual = 8.05412e-07, No Iterations 127 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.41318e-09, global = -1.10838e-13, cumulative = 9.38082e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.00460597, Final residual = 3.10221e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00145197, Final residual = 1.30223e-06, No Iterations 3 Mean pressure:406750 Mean temperature:549.728 Mean u':0.306879 ExecutionTime = 2766.29 s ClockTime = 2879 s Courant Number mean: 0.0223485 max: 0.138166 deltaT = 0.000833367 Crank angle = -54.1667 CA-deg deltaZ = 0.000682896 clearance: 0.0355481 Piston speed = 0.819442 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.28491, Final residual = 1.45044e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.209493, Final residual = 7.78416e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0134965, Final residual = 6.33915e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000189894, Final residual = 9.23571e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.443402, Final residual = 9.50542e-07, No Iterations 5 T gas min/max = 433, 561.964 DICPCG: Solving for p, Initial residual = 0.97313, Final residual = 0.0954283, No Iterations 54 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00247609, global = 1.28424e-07, cumulative = 9.50924e-06 DICPCG: Solving for p, Initial residual = 0.886932, Final residual = 9.97672e-07, No Iterations 126 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.62001e-09, global = -5.90758e-15, cumulative = 9.50924e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.00396799, Final residual = 1.40876e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00133877, Final residual = 7.67393e-06, No Iterations 2 Mean pressure:417287 Mean temperature:553.34 Mean u':0.307007 ExecutionTime = 2781.08 s ClockTime = 2894 s Courant Number mean: 0.0186907 max: 0.116916 deltaT = 0.000833367 Crank angle = -53.3333 CA-deg deltaZ = 0.000678528 clearance: 0.0348696 Piston speed = 0.814201 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.221893, Final residual = 9.96972e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.308803, Final residual = 1.59852e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0136088, Final residual = 5.63665e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000190623, Final residual = 9.67396e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.441213, Final residual = 9.72765e-07, No Iterations 5 T gas min/max = 433, 565.635 DICPCG: Solving for p, Initial residual = 0.971008, Final residual = 0.0911096, No Iterations 54 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.0023989, global = 1.36774e-07, cumulative = 9.64601e-06 DICPCG: Solving for p, Initial residual = 0.88873, Final residual = 8.52407e-07, No Iterations 128 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.04898e-09, global = 1.62377e-14, cumulative = 9.64601e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.00408799, Final residual = 1.69018e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00146963, Final residual = 9.0107e-06, No Iterations 2 Mean pressure:428235 Mean temperature:557.021 Mean u':0.307158 ExecutionTime = 2795.94 s ClockTime = 2909 s Courant Number mean: 0.0190875 max: 0.120107 deltaT = 0.000833367 Crank angle = -52.5 CA-deg deltaZ = 0.000673916 clearance: 0.0341956 Piston speed = 0.808666 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.316549, Final residual = 1.62815e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.239455, Final residual = 9.81898e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0141181, Final residual = 6.70399e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000192185, Final residual = 1.26463e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.43829, Final residual = 9.94658e-07, No Iterations 5 T gas min/max = 433, 569.367 DICPCG: Solving for p, Initial residual = 0.971871, Final residual = 0.0803436, No Iterations 57 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00213904, global = 3.52943e-08, cumulative = 9.68131e-06 DICPCG: Solving for p, Initial residual = 0.845701, Final residual = 9.4848e-07, No Iterations 127 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.98225e-09, global = 5.11124e-14, cumulative = 9.68131e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.00424077, Final residual = 2.18041e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00156632, Final residual = 1.03817e-06, No Iterations 3 Mean pressure:439610 Mean temperature:560.767 Mean u':0.307324 ExecutionTime = 2810.73 s ClockTime = 2923 s Courant Number mean: 0.0191284 max: 0.120126 deltaT = 0.000833367 Crank angle = -51.6667 CA-deg deltaZ = 0.000669059 clearance: 0.0335266 Piston speed = 0.802839 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.195673, Final residual = 8.04723e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.229932, Final residual = 8.92407e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.00918961, Final residual = 3.86798e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000194339, Final residual = 1.42598e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.434939, Final residual = 1.01636e-06, No Iterations 5 T gas min/max = 433, 573.154 DICPCG: Solving for p, Initial residual = 0.973088, Final residual = 0.0861926, No Iterations 53 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00231893, global = 9.26653e-08, cumulative = 9.77397e-06 DICPCG: Solving for p, Initial residual = 0.863437, Final residual = 9.86939e-07, No Iterations 129 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.3227e-09, global = 1.87225e-14, cumulative = 9.77397e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.00446805, Final residual = 2.66684e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0016775, Final residual = 1.12695e-06, No Iterations 3 Mean pressure:451429 Mean temperature:564.578 Mean u':0.307509 ExecutionTime = 2825.54 s ClockTime = 2938 s Courant Number mean: 0.0196304 max: 0.125293 deltaT = 0.000833367 Crank angle = -50.8333 CA-deg deltaZ = 0.00066396 clearance: 0.0328626 Piston speed = 0.796721 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.320713, Final residual = 1.65077e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.214187, Final residual = 8.47781e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0121301, Final residual = 3.26582e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000192031, Final residual = 1.47759e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.431235, Final residual = 1.03339e-06, No Iterations 5 T gas min/max = 433, 576.999 DICPCG: Solving for p, Initial residual = 0.971951, Final residual = 0.0882234, No Iterations 53 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00240388, global = 1.84001e-07, cumulative = 9.95798e-06 DICPCG: Solving for p, Initial residual = 0.865399, Final residual = 8.00599e-07, No Iterations 133 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.83832e-09, global = 2.6852e-14, cumulative = 9.95798e-06 DILUPBiCG: Solving for epsilon, Initial residual = 0.00477073, Final residual = 3.15775e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00175638, Final residual = 1.236e-06, No Iterations 3 Mean pressure:463709 Mean temperature:568.454 Mean u':0.307709 ExecutionTime = 2840.33 s ClockTime = 2953 s Courant Number mean: 0.0197951 max: 0.126931 deltaT = 0.000833367 Crank angle = -50 CA-deg deltaZ = 0.00065862 clearance: 0.032204 Piston speed = 0.790312 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.25598, Final residual = 9.07626e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.372597, Final residual = 1.37037e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.016604, Final residual = 5.61294e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000189199, Final residual = 1.33853e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.42718, Final residual = 1.05343e-06, No Iterations 5 T gas min/max = 433, 580.908 DICPCG: Solving for p, Initial residual = 0.970609, Final residual = 0.0889826, No Iterations 57 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00245556, global = 6.41304e-08, cumulative = 1.00221e-05 DICPCG: Solving for p, Initial residual = 0.852627, Final residual = 8.16063e-07, No Iterations 130 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 2.93628e-09, global = 1.23447e-13, cumulative = 1.00221e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.00509228, Final residual = 3.6918e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00184041, Final residual = 1.26843e-06, No Iterations 3 Mean pressure:476471 Mean temperature:572.395 Mean u':0.307921 ExecutionTime = 2856.88 s ClockTime = 2973 s Courant Number mean: 0.0199707 max: 0.126685 deltaT = 0.00100004 Crank angle = -49 CA-deg deltaZ = 0.000782956 clearance: 0.031421 Piston speed = 0.782925 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.328773, Final residual = 4.09885e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.260504, Final residual = 3.2192e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0169723, Final residual = 1.45384e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000214453, Final residual = 7.56962e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.474403, Final residual = 2.88425e-06, No Iterations 5 T gas min/max = 433, 585.661 DICPCG: Solving for p, Initial residual = 0.966586, Final residual = 0.0953219, No Iterations 59 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00319488, global = 7.69728e-08, cumulative = 1.00991e-05 DICPCG: Solving for p, Initial residual = 0.867585, Final residual = 8.43617e-07, No Iterations 134 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.1992e-09, global = -1.33329e-13, cumulative = 1.00991e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.00645536, Final residual = 8.40542e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00227889, Final residual = 2.68261e-06, No Iterations 3 Mean pressure:492424 Mean temperature:577.18 Mean u':0.308188 ExecutionTime = 2871.72 s ClockTime = 2987 s Courant Number mean: 0.0241808 max: 0.151912 deltaT = 0.00100004 Crank angle = -48 CA-deg deltaZ = 0.000774508 clearance: 0.0306465 Piston speed = 0.774477 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.288896, Final residual = 3.28997e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.344762, Final residual = 3.71653e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.018251, Final residual = 1.64186e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000213304, Final residual = 2.05812e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.468091, Final residual = 2.92989e-06, No Iterations 5 T gas min/max = 433, 590.511 DICPCG: Solving for p, Initial residual = 0.966513, Final residual = 0.0803648, No Iterations 61 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00272802, global = 3.10142e-08, cumulative = 1.01301e-05 DICPCG: Solving for p, Initial residual = 0.825082, Final residual = 8.44901e-07, No Iterations 134 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.82574e-09, global = 2.58899e-14, cumulative = 1.01301e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.00697262, Final residual = 9.6378e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00234045, Final residual = 2.75452e-06, No Iterations 3 Mean pressure:509128 Mean temperature:582.052 Mean u':0.308467 ExecutionTime = 2886.72 s ClockTime = 3002 s Courant Number mean: 0.0247136 max: 0.150408 deltaT = 0.00100004 Crank angle = -47 CA-deg deltaZ = 0.000765651 clearance: 0.0298809 Piston speed = 0.765621 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.264587, Final residual = 3.33476e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.230174, Final residual = 2.9892e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0179536, Final residual = 1.61952e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000212978, Final residual = 5.21565e-07, No Iterations 3 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.46146, Final residual = 2.95211e-06, No Iterations 5 T gas min/max = 433, 595.448 DICPCG: Solving for p, Initial residual = 0.967888, Final residual = 0.0925302, No Iterations 59 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00317619, global = 8.11384e-08, cumulative = 1.02112e-05 DICPCG: Solving for p, Initial residual = 0.834433, Final residual = 8.67975e-07, No Iterations 135 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.28629e-09, global = -7.93888e-14, cumulative = 1.02112e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.00749301, Final residual = 1.59259e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.00234721, Final residual = 2.81386e-06, No Iterations 3 Mean pressure:526625 Mean temperature:587.017 Mean u':0.30875 ExecutionTime = 2901.61 s ClockTime = 3017 s Courant Number mean: 0.0249183 max: 0.152045 deltaT = 0.00100004 Crank angle = -46 CA-deg deltaZ = 0.00075639 clearance: 0.0291245 Piston speed = 0.75636 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.267854, Final residual = 2.9468e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.338139, Final residual = 3.41295e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0177318, Final residual = 1.76707e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000222204, Final residual = 2.75893e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.454323, Final residual = 2.96183e-06, No Iterations 5 T gas min/max = 433, 600.463 DICPCG: Solving for p, Initial residual = 0.965248, Final residual = 0.0896158, No Iterations 61 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00312268, global = 5.37827e-08, cumulative = 1.0265e-05 DICPCG: Solving for p, Initial residual = 0.82363, Final residual = 9.22391e-07, No Iterations 135 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.54892e-09, global = 2.05708e-13, cumulative = 1.0265e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.00800091, Final residual = 1.78253e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.00237806, Final residual = 2.6125e-06, No Iterations 3 Mean pressure:544954 Mean temperature:592.075 Mean u':0.309038 ExecutionTime = 2916.52 s ClockTime = 3032 s Courant Number mean: 0.0255701 max: 0.155062 deltaT = 0.00100004 Crank angle = -45 CA-deg deltaZ = 0.000746727 clearance: 0.0283778 Piston speed = 0.746697 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.279044, Final residual = 3.13424e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.234984, Final residual = 2.99059e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0244693, Final residual = 2.26661e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.0002098, Final residual = 1.64903e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.446653, Final residual = 2.94737e-06, No Iterations 5 T gas min/max = 433, 605.568 DICPCG: Solving for p, Initial residual = 0.965691, Final residual = 0.092455, No Iterations 60 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00325876, global = 9.37665e-08, cumulative = 1.03588e-05 DICPCG: Solving for p, Initial residual = 0.83682, Final residual = 8.38205e-07, No Iterations 136 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.46974e-09, global = 1.27234e-13, cumulative = 1.03588e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.00847415, Final residual = 1.9781e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.00233358, Final residual = 2.51965e-06, No Iterations 3 Mean pressure:564156 Mean temperature:597.227 Mean u':0.309322 ExecutionTime = 2933.06 s ClockTime = 3056 s Courant Number mean: 0.0257615 max: 0.15068 deltaT = 0.000833367 Crank angle = -44.1667 CA-deg deltaZ = 0.000614605 clearance: 0.0277632 Piston speed = 0.737497 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.234396, Final residual = 8.58295e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.264506, Final residual = 1.28253e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0167892, Final residual = 9.27957e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000188539, Final residual = 1.06606e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.388019, Final residual = 1.06888e-06, No Iterations 5 T gas min/max = 433, 609.913 DICPCG: Solving for p, Initial residual = 0.967025, Final residual = 0.088591, No Iterations 58 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00263809, global = 8.89887e-08, cumulative = 1.04478e-05 DICPCG: Solving for p, Initial residual = 0.81352, Final residual = 8.11028e-07, No Iterations 133 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.38974e-09, global = 1.00095e-13, cumulative = 1.04478e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.00756421, Final residual = 7.48099e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00191318, Final residual = 1.13241e-06, No Iterations 3 Mean pressure:580884 Mean temperature:601.62 Mean u':0.309553 ExecutionTime = 2947.93 s ClockTime = 3071 s Courant Number mean: 0.0219659 max: 0.127937 deltaT = 0.000833367 Crank angle = -43.3333 CA-deg deltaZ = 0.000607393 clearance: 0.0271558 Piston speed = 0.728842 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.299676, Final residual = 1.26286e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.24492, Final residual = 1.14334e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.018692, Final residual = 8.03162e-07, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000190019, Final residual = 6.72551e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.381297, Final residual = 1.05356e-06, No Iterations 5 T gas min/max = 433, 614.337 DICPCG: Solving for p, Initial residual = 0.964141, Final residual = 0.0753359, No Iterations 61 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00227185, global = 4.17759e-08, cumulative = 1.04895e-05 DICPCG: Solving for p, Initial residual = 0.798492, Final residual = 8.90159e-07, No Iterations 121 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.42022e-09, global = 2.23531e-13, cumulative = 1.04895e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.00787626, Final residual = 8.02964e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00187276, Final residual = 9.58827e-07, No Iterations 3 Mean pressure:598279 Mean temperature:606.084 Mean u':0.309774 ExecutionTime = 2962.74 s ClockTime = 3086 s Courant Number mean: 0.0221729 max: 0.127749 deltaT = 0.000833367 Crank angle = -42.5 CA-deg deltaZ = 0.000599956 clearance: 0.0265558 Piston speed = 0.719918 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.173135, Final residual = 6.49949e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.18025, Final residual = 8.29036e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0204877, Final residual = 9.47867e-07, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.00018904, Final residual = 4.85898e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.373708, Final residual = 1.03783e-06, No Iterations 5 T gas min/max = 433, 618.88 DICPCG: Solving for p, Initial residual = 0.965958, Final residual = 0.0881187, No Iterations 54 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00267656, global = 1.45195e-07, cumulative = 1.06347e-05 DICPCG: Solving for p, Initial residual = 0.800475, Final residual = 9.99803e-07, No Iterations 133 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.2642e-09, global = 1.42205e-13, cumulative = 1.06347e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.00817103, Final residual = 8.53301e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00184649, Final residual = 9.76988e-07, No Iterations 3 Mean pressure:616363 Mean temperature:610.613 Mean u':0.309985 ExecutionTime = 2977.63 s ClockTime = 3101 s Courant Number mean: 0.0228187 max: 0.133757 deltaT = 0.000833367 Crank angle = -41.6667 CA-deg deltaZ = 0.000592297 clearance: 0.0259635 Piston speed = 0.710728 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.334128, Final residual = 1.28558e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.270571, Final residual = 1.09958e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0161529, Final residual = 9.54596e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000190182, Final residual = 1.59953e-07, No Iterations 3 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.365817, Final residual = 1.01305e-06, No Iterations 5 T gas min/max = 433, 623.607 DICPCG: Solving for p, Initial residual = 0.962995, Final residual = 0.0895249, No Iterations 57 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00275147, global = 1.2913e-07, cumulative = 1.07639e-05 DICPCG: Solving for p, Initial residual = 0.796175, Final residual = 9.55051e-07, No Iterations 137 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.13493e-09, global = 3.93595e-14, cumulative = 1.07639e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.00844795, Final residual = 9.03997e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00175745, Final residual = 8.87272e-07, No Iterations 3 Mean pressure:635162 Mean temperature:615.206 Mean u':0.310177 ExecutionTime = 2992.51 s ClockTime = 3116 s Courant Number mean: 0.0229769 max: 0.129832 deltaT = 0.000833367 Crank angle = -40.8333 CA-deg deltaZ = 0.000584419 clearance: 0.0253791 Piston speed = 0.701274 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.277534, Final residual = 9.35291e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.323146, Final residual = 1.09078e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0206627, Final residual = 8.98284e-07, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000192158, Final residual = 6.53757e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.357757, Final residual = 9.91203e-07, No Iterations 5 T gas min/max = 433, 628.396 DICPCG: Solving for p, Initial residual = 0.962723, Final residual = 0.0915994, No Iterations 59 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.0028396, global = 8.83772e-08, cumulative = 1.08522e-05 DICPCG: Solving for p, Initial residual = 0.796763, Final residual = 6.98226e-07, No Iterations 135 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.09974e-09, global = -1.90035e-13, cumulative = 1.08522e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.0087008, Final residual = 9.47076e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.00171691, Final residual = 1.03624e-06, No Iterations 3 Mean pressure:654701 Mean temperature:619.862 Mean u':0.31035 ExecutionTime = 3007.36 s ClockTime = 3131 s Courant Number mean: 0.0233982 max: 0.13072 deltaT = 0.000833367 Crank angle = -40 CA-deg deltaZ = 0.000576324 clearance: 0.0248028 Piston speed = 0.691561 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.289079, Final residual = 1.22935e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.25126, Final residual = 9.89401e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0175388, Final residual = 8.08784e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000192926, Final residual = 6.21599e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.349632, Final residual = 9.53127e-07, No Iterations 5 T gas min/max = 433, 633.249 DICPCG: Solving for p, Initial residual = 0.961523, Final residual = 0.0907412, No Iterations 60 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00283903, global = 1.01763e-07, cumulative = 1.0954e-05 DICPCG: Solving for p, Initial residual = 0.789034, Final residual = 9.27311e-07, No Iterations 135 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.26769e-09, global = 1.94974e-13, cumulative = 1.0954e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.00895172, Final residual = 9.94432e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0016669, Final residual = 1.21845e-06, No Iterations 3 Mean pressure:675007 Mean temperature:624.58 Mean u':0.310496 ExecutionTime = 3023.96 s ClockTime = 3150 s Courant Number mean: 0.0236012 max: 0.129655 deltaT = 0.00100004 Crank angle = -39 CA-deg deltaZ = 0.000680602 clearance: 0.0241222 Piston speed = 0.680575 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.288179, Final residual = 2.39302e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.358302, Final residual = 3.05215e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0192633, Final residual = 1.55061e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000210628, Final residual = 1.83241e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.388567, Final residual = 2.57245e-06, No Iterations 5 T gas min/max = 433, 639.124 DICPCG: Solving for p, Initial residual = 0.956678, Final residual = 0.0938987, No Iterations 65 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00355605, global = 2.57035e-08, cumulative = 1.09797e-05 DICPCG: Solving for p, Initial residual = 0.787456, Final residual = 8.5933e-07, No Iterations 135 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.12548e-09, global = -2.73763e-14, cumulative = 1.09797e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.0107825, Final residual = 2.94193e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.00198678, Final residual = 3.15052e-06, No Iterations 3 Mean pressure:700383 Mean temperature:630.283 Mean u':0.31063 ExecutionTime = 3038.87 s ClockTime = 3165 s Courant Number mean: 0.0285952 max: 0.156 deltaT = 0.00100004 Crank angle = -38 CA-deg deltaZ = 0.000668274 clearance: 0.0234539 Piston speed = 0.668247 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.256618, Final residual = 2.48233e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.236392, Final residual = 2.3434e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0192166, Final residual = 1.61372e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000207408, Final residual = 1.89568e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.377878, Final residual = 2.44496e-06, No Iterations 5 T gas min/max = 433, 645.081 DICPCG: Solving for p, Initial residual = 0.957586, Final residual = 0.0953604, No Iterations 62 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00363788, global = 1.11368e-07, cumulative = 1.10911e-05 DICPCG: Solving for p, Initial residual = 0.772622, Final residual = 8.45249e-07, No Iterations 138 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.18756e-09, global = 3.25431e-14, cumulative = 1.10911e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.0110554, Final residual = 3.04506e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.00204667, Final residual = 3.52667e-06, No Iterations 3 Mean pressure:726938 Mean temperature:636.064 Mean u':0.310712 ExecutionTime = 3053.86 s ClockTime = 3180 s Courant Number mean: 0.0290228 max: 0.154252 deltaT = 0.00100004 Crank angle = -37 CA-deg deltaZ = 0.000655588 clearance: 0.0227983 Piston speed = 0.655562 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.273956, Final residual = 2.11185e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.353709, Final residual = 2.8072e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0210575, Final residual = 1.60746e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000210593, Final residual = 1.55816e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.367446, Final residual = 2.32276e-06, No Iterations 5 T gas min/max = 433, 651.117 DICPCG: Solving for p, Initial residual = 0.955634, Final residual = 0.0827697, No Iterations 66 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00318873, global = 1.91251e-08, cumulative = 1.11102e-05 DICPCG: Solving for p, Initial residual = 0.738608, Final residual = 8.17766e-07, No Iterations 137 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.73799e-09, global = -3.79218e-14, cumulative = 1.11102e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.0112796, Final residual = 3.095e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.00217919, Final residual = 4.33339e-06, No Iterations 3 Mean pressure:754724 Mean temperature:641.925 Mean u':0.310731 ExecutionTime = 3068.85 s ClockTime = 3195 s Courant Number mean: 0.0288977 max: 0.147189 deltaT = 0.00100004 Crank angle = -36 CA-deg deltaZ = 0.000642551 clearance: 0.0221558 Piston speed = 0.642526 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.195483, Final residual = 1.48523e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.178124, Final residual = 1.4963e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0233807, Final residual = 1.83096e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000210783, Final residual = 2.56744e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.357104, Final residual = 2.18206e-06, No Iterations 5 T gas min/max = 433, 657.31 DICPCG: Solving for p, Initial residual = 0.955446, Final residual = 0.0923522, No Iterations 62 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00358407, global = 8.58698e-08, cumulative = 1.11961e-05 DICPCG: Solving for p, Initial residual = 0.73478, Final residual = 8.76917e-07, No Iterations 141 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.42709e-09, global = -4.30704e-14, cumulative = 1.11961e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.0114666, Final residual = 3.12561e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.00247152, Final residual = 4.87289e-06, No Iterations 3 Mean pressure:783787 Mean temperature:647.863 Mean u':0.310681 ExecutionTime = 3083.9 s ClockTime = 3210 s Courant Number mean: 0.0293061 max: 0.150226 deltaT = 0.00100004 Crank angle = -35 CA-deg deltaZ = 0.000629171 clearance: 0.0215266 Piston speed = 0.629145 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.262646, Final residual = 1.59978e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.306813, Final residual = 2.12014e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0221997, Final residual = 1.14148e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000212674, Final residual = 1.04235e-06, No Iterations 3 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.346721, Final residual = 2.03193e-06, No Iterations 5 T gas min/max = 433, 663.648 DICPCG: Solving for p, Initial residual = 0.952618, Final residual = 0.0767406, No Iterations 66 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00300622, global = 2.53114e-08, cumulative = 1.12214e-05 DICPCG: Solving for p, Initial residual = 0.678698, Final residual = 9.53936e-07, No Iterations 136 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.3797e-09, global = 6.31749e-14, cumulative = 1.12214e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.0116114, Final residual = 3.11511e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.00281433, Final residual = 5.39362e-06, No Iterations 3 Mean pressure:814170 Mean temperature:653.875 Mean u':0.31055 ExecutionTime = 3100.54 s ClockTime = 3230 s Courant Number mean: 0.0291596 max: 0.146825 deltaT = 0.000833367 Crank angle = -34.1667 CA-deg deltaZ = 0.000513844 clearance: 0.0210127 Piston speed = 0.616588 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.166421, Final residual = 5.43735e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.15894, Final residual = 6.01669e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0208396, Final residual = 8.50729e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000192153, Final residual = 3.07887e-07, No Iterations 3 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.293331, Final residual = 8.4809e-06, No Iterations 4 T gas min/max = 433, 669.025 DICPCG: Solving for p, Initial residual = 0.958539, Final residual = 0.092231, No Iterations 58 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.0030222, global = 1.30257e-07, cumulative = 1.13516e-05 DICPCG: Solving for p, Initial residual = 0.712752, Final residual = 8.68182e-07, No Iterations 140 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.51579e-09, global = -4.05974e-14, cumulative = 1.13516e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.00996668, Final residual = 1.29543e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.00273856, Final residual = 2.99059e-06, No Iterations 3 Mean pressure:840571 Mean temperature:658.971 Mean u':0.310376 ExecutionTime = 3115.42 s ClockTime = 3245 s Courant Number mean: 0.0246239 max: 0.123299 deltaT = 0.000833367 Crank angle = -33.3333 CA-deg deltaZ = 0.000504127 clearance: 0.0205086 Piston speed = 0.604928 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.241477, Final residual = 7.16894e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.290159, Final residual = 9.45354e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0238056, Final residual = 8.20004e-07, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000184285, Final residual = 8.85291e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.285506, Final residual = 7.947e-06, No Iterations 4 T gas min/max = 433, 674.456 DICPCG: Solving for p, Initial residual = 0.950567, Final residual = 0.0857844, No Iterations 61 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00284638, global = 6.27931e-08, cumulative = 1.14144e-05 DICPCG: Solving for p, Initial residual = 0.713444, Final residual = 9.00088e-07, No Iterations 135 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.5751e-09, global = 8.21487e-14, cumulative = 1.14144e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.0100159, Final residual = 1.26661e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.00312948, Final residual = 3.23489e-06, No Iterations 3 Mean pressure:867947 Mean temperature:664.116 Mean u':0.310133 ExecutionTime = 3130.27 s ClockTime = 3260 s Courant Number mean: 0.0243483 max: 0.121777 deltaT = 0.000833367 Crank angle = -32.5 CA-deg deltaZ = 0.000494222 clearance: 0.0200144 Piston speed = 0.593042 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.219459, Final residual = 6.62952e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.203902, Final residual = 6.23473e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.019423, Final residual = 8.71822e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000183156, Final residual = 1.01592e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.2777, Final residual = 7.43e-06, No Iterations 4 T gas min/max = 433, 679.967 DICPCG: Solving for p, Initial residual = 0.952619, Final residual = 0.0831482, No Iterations 61 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00276241, global = 9.28538e-08, cumulative = 1.15073e-05 DICPCG: Solving for p, Initial residual = 0.707111, Final residual = 8.25438e-07, No Iterations 141 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.1521e-09, global = -9.68076e-14, cumulative = 1.15073e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.0100492, Final residual = 1.2328e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.00360875, Final residual = 3.62345e-06, No Iterations 3 Mean pressure:896314 Mean temperature:669.303 Mean u':0.309822 ExecutionTime = 3145.16 s ClockTime = 3274 s Courant Number mean: 0.0248984 max: 0.125781 deltaT = 0.000833367 Crank angle = -31.6667 CA-deg deltaZ = 0.000484133 clearance: 0.0195303 Piston speed = 0.580936 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.215839, Final residual = 6.35855e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.276721, Final residual = 8.0497e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0257754, Final residual = 7.34017e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000183688, Final residual = 5.33612e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.269977, Final residual = 6.91073e-06, No Iterations 4 T gas min/max = 433, 685.549 DICPCG: Solving for p, Initial residual = 0.952803, Final residual = 0.087249, No Iterations 63 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00290594, global = 7.21707e-08, cumulative = 1.15795e-05 DICPCG: Solving for p, Initial residual = 0.693963, Final residual = 8.29664e-07, No Iterations 145 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.25665e-09, global = -8.88774e-14, cumulative = 1.15795e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.0100427, Final residual = 1.18941e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0041321, Final residual = 4.01352e-06, No Iterations 3 Mean pressure:925690 Mean temperature:674.527 Mean u':0.309433 ExecutionTime = 3160.04 s ClockTime = 3289 s Courant Number mean: 0.0250789 max: 0.127841 deltaT = 0.000833367 Crank angle = -30.8333 CA-deg deltaZ = 0.000473864 clearance: 0.0190564 Piston speed = 0.568614 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.258998, Final residual = 7.80073e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.224752, Final residual = 7.0693e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.028685, Final residual = 9.75558e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000179759, Final residual = 8.81392e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.262351, Final residual = 6.43001e-06, No Iterations 4 T gas min/max = 433, 691.174 DICPCG: Solving for p, Initial residual = 0.950077, Final residual = 0.0930985, No Iterations 64 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00311575, global = 9.14458e-08, cumulative = 1.16709e-05 DICPCG: Solving for p, Initial residual = 0.690887, Final residual = 8.90537e-07, No Iterations 141 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.93287e-09, global = -1.3344e-14, cumulative = 1.16709e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.0100169, Final residual = 1.13769e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.00473055, Final residual = 4.33411e-06, No Iterations 3 Mean pressure:956090 Mean temperature:679.785 Mean u':0.308965 ExecutionTime = 3174.96 s ClockTime = 3304 s Courant Number mean: 0.0252182 max: 0.125743 deltaT = 0.000833367 Crank angle = -30 CA-deg deltaZ = 0.000463419 clearance: 0.018593 Piston speed = 0.55608 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.240332, Final residual = 6.14212e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.30223, Final residual = 8.80084e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0210851, Final residual = 7.19913e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000181762, Final residual = 1.19094e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.254809, Final residual = 5.9106e-06, No Iterations 4 T gas min/max = 433, 696.838 DICPCG: Solving for p, Initial residual = 0.947308, Final residual = 0.0793014, No Iterations 67 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00266485, global = 2.97129e-08, cumulative = 1.17006e-05 DICPCG: Solving for p, Initial residual = 0.658806, Final residual = 9.85369e-07, No Iterations 143 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.01451e-09, global = 1.12631e-13, cumulative = 1.17006e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.0099458, Final residual = 1.07956e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.00540412, Final residual = 4.78168e-06, No Iterations 3 Mean pressure:987527 Mean temperature:685.071 Mean u':0.308406 ExecutionTime = 3191.54 s ClockTime = 3325 s Courant Number mean: 0.0252375 max: 0.122556 deltaT = 0.00100004 Crank angle = -29 CA-deg deltaZ = 0.000542072 clearance: 0.0180509 Piston speed = 0.54205 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.213471, Final residual = 1.04399e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.192223, Final residual = 9.87602e-07, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0290399, Final residual = 1.7355e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000203235, Final residual = 1.01915e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.284626, Final residual = 1.14694e-06, No Iterations 5 T gas min/max = 433, 703.642 DICPCG: Solving for p, Initial residual = 0.943012, Final residual = 0.0872057, No Iterations 66 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00351683, global = 9.87362e-08, cumulative = 1.17994e-05 DICPCG: Solving for p, Initial residual = 0.660234, Final residual = 8.63426e-07, No Iterations 151 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.8448e-09, global = -6.24736e-15, cumulative = 1.17994e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.0115909, Final residual = 2.45861e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.00734081, Final residual = 1.01666e-06, No Iterations 4 Mean pressure:1.02657e+06 Mean temperature:691.405 Mean u':0.307622 ExecutionTime = 3206.53 s ClockTime = 3340 s Courant Number mean: 0.0309958 max: 0.151977 deltaT = 0.00100004 Crank angle = -28 CA-deg deltaZ = 0.000526493 clearance: 0.0175244 Piston speed = 0.526472 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.272777, Final residual = 1.06891e-06, No Iterations 5 DILUPBiCG: Solving for Uy, Initial residual = 0.318571, Final residual = 1.41275e-06, No Iterations 5 DILUPBiCG: Solving for Uz, Initial residual = 0.0251356, Final residual = 1.35456e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000204394, Final residual = 8.10816e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.274661, Final residual = 1.01164e-06, No Iterations 5 T gas min/max = 433, 710.484 DICPCG: Solving for p, Initial residual = 0.944279, Final residual = 0.0663966, No Iterations 72 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.0026717, global = 1.27064e-08, cumulative = 1.18121e-05 DICPCG: Solving for p, Initial residual = 0.567463, Final residual = 8.09705e-07, No Iterations 146 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.08083e-09, global = 6.09976e-14, cumulative = 1.18121e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.0113815, Final residual = 2.24886e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.00853254, Final residual = 1.10316e-06, No Iterations 4 Mean pressure:1.06711e+06 Mean temperature:697.764 Mean u':0.306687 ExecutionTime = 3221.61 s ClockTime = 3355 s Courant Number mean: 0.0303938 max: 0.153072 deltaT = 0.00100004 Crank angle = -27 CA-deg deltaZ = 0.000510631 clearance: 0.0170138 Piston speed = 0.510611 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.15087, Final residual = 7.00944e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.145674, Final residual = 5.99412e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0262424, Final residual = 1.11956e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000196962, Final residual = 5.15454e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.264774, Final residual = 8.85597e-07, No Iterations 5 T gas min/max = 433, 717.356 DICPCG: Solving for p, Initial residual = 0.943205, Final residual = 0.0773673, No Iterations 65 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00310948, global = 5.42263e-08, cumulative = 1.18663e-05 DICPCG: Solving for p, Initial residual = 0.581085, Final residual = 9.87822e-07, No Iterations 153 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 6.59354e-09, global = 1.69933e-13, cumulative = 1.18663e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.011102, Final residual = 2.03e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.00975669, Final residual = 1.17243e-06, No Iterations 4 Mean pressure:1.10916e+06 Mean temperature:704.139 Mean u':0.305607 ExecutionTime = 3236.62 s ClockTime = 3370 s Courant Number mean: 0.0309261 max: 0.156823 deltaT = 0.00100004 Crank angle = -26 CA-deg deltaZ = 0.000494496 clearance: 0.0165193 Piston speed = 0.494477 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.209537, Final residual = 8.16748e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.237264, Final residual = 9.82094e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0333262, Final residual = 1.4559e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000197163, Final residual = 1.60858e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.254938, Final residual = 9.27858e-06, No Iterations 4 T gas min/max = 433, 724.248 DICPCG: Solving for p, Initial residual = 0.938964, Final residual = 0.0836249, No Iterations 71 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00336307, global = 1.9879e-08, cumulative = 1.18862e-05 DICPCG: Solving for p, Initial residual = 0.594405, Final residual = 8.5851e-07, No Iterations 149 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 6.14969e-09, global = -5.28112e-14, cumulative = 1.18862e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.0107697, Final residual = 1.81995e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0111489, Final residual = 1.24145e-06, No Iterations 4 Mean pressure:1.15269e+06 Mean temperature:710.519 Mean u':0.304364 ExecutionTime = 3251.67 s ClockTime = 3385 s Courant Number mean: 0.0303356 max: 0.155431 deltaT = 0.00100004 Crank angle = -25 CA-deg deltaZ = 0.000478097 clearance: 0.0160412 Piston speed = 0.478078 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.168509, Final residual = 5.12574e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.14076, Final residual = 5.79001e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0357719, Final residual = 1.36262e-06, No Iterations 4 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000189849, Final residual = 1.29769e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.245143, Final residual = 8.19798e-06, No Iterations 4 T gas min/max = 433, 731.147 DICPCG: Solving for p, Initial residual = 0.937127, Final residual = 0.0776311, No Iterations 67 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00311067, global = 4.72964e-08, cumulative = 1.19335e-05 DICPCG: Solving for p, Initial residual = 0.551255, Final residual = 8.669e-07, No Iterations 156 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 6.0493e-09, global = 9.06181e-15, cumulative = 1.19335e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.0103593, Final residual = 1.6152e-06, No Iterations 4 DILUPBiCG: Solving for k, Initial residual = 0.0125727, Final residual = 1.29215e-06, No Iterations 4 Mean pressure:1.19766e+06 Mean temperature:716.891 Mean u':0.30296 ExecutionTime = 3268.29 s ClockTime = 3406 s Courant Number mean: 0.0307656 max: 0.15927 deltaT = 0.000833367 Crank angle = -24.1667 CA-deg deltaZ = 0.000385702 clearance: 0.0156555 Piston speed = 0.462824 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.179092, Final residual = 2.8012e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.194313, Final residual = 3.04693e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.027837, Final residual = 7.22647e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000165026, Final residual = 7.23514e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.20386, Final residual = 2.93346e-06, No Iterations 4 T gas min/max = 433, 736.923 DICPCG: Solving for p, Initial residual = 0.941133, Final residual = 0.0874151, No Iterations 65 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.0029, global = 8.52565e-08, cumulative = 1.20187e-05 DICPCG: Solving for p, Initial residual = 0.576778, Final residual = 9.28477e-07, No Iterations 155 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.67715e-09, global = -2.05564e-14, cumulative = 1.20187e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.00836735, Final residual = 6.69842e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0118579, Final residual = 7.53758e-06, No Iterations 3 Mean pressure:1.23626e+06 Mean temperature:722.216 Mean u':0.301652 ExecutionTime = 3283.3 s ClockTime = 3421 s Courant Number mean: 0.025391 max: 0.133721 deltaT = 0.000833367 Crank angle = -23.3333 CA-deg deltaZ = 0.000373993 clearance: 0.0152815 Piston speed = 0.448773 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.260884, Final residual = 3.85394e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.236937, Final residual = 3.41171e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0319872, Final residual = 6.57228e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.0001662, Final residual = 5.51351e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.196477, Final residual = 2.60496e-06, No Iterations 4 T gas min/max = 433, 742.679 DICPCG: Solving for p, Initial residual = 0.933012, Final residual = 0.0923255, No Iterations 71 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00306499, global = 3.21881e-08, cumulative = 1.20509e-05 DICPCG: Solving for p, Initial residual = 0.591218, Final residual = 9.59723e-07, No Iterations 155 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 6.00707e-09, global = 3.30568e-13, cumulative = 1.20509e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.00798456, Final residual = 6.07109e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0130012, Final residual = 7.78145e-06, No Iterations 3 Mean pressure:1.27577e+06 Mean temperature:727.512 Mean u':0.300221 ExecutionTime = 3298.31 s ClockTime = 3436 s Courant Number mean: 0.0254559 max: 0.131034 deltaT = 0.000833367 Crank angle = -22.5 CA-deg deltaZ = 0.000362144 clearance: 0.0149194 Piston speed = 0.434556 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.17265, Final residual = 2.38222e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.205253, Final residual = 2.86497e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0307534, Final residual = 5.7587e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000163812, Final residual = 4.60286e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.189224, Final residual = 2.29971e-06, No Iterations 4 T gas min/max = 433, 748.405 DICPCG: Solving for p, Initial residual = 0.931397, Final residual = 0.0930141, No Iterations 56 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00306432, global = 2.86706e-07, cumulative = 1.23376e-05 DICPCG: Solving for p, Initial residual = 0.591228, Final residual = 8.98894e-07, No Iterations 158 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.65463e-09, global = -7.86737e-14, cumulative = 1.23376e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.00754049, Final residual = 5.4186e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0140744, Final residual = 7.88334e-06, No Iterations 3 Mean pressure:1.31616e+06 Mean temperature:732.771 Mean u':0.29868 ExecutionTime = 3313.24 s ClockTime = 3451 s Courant Number mean: 0.0270028 max: 0.134499 deltaT = 0.000833367 Crank angle = -21.6667 CA-deg deltaZ = 0.000350162 clearance: 0.0145692 Piston speed = 0.420177 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.351387, Final residual = 4.02682e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.278856, Final residual = 3.04775e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0311007, Final residual = 6.50849e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000163796, Final residual = 8.68865e-08, No Iterations 3 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.182, Final residual = 2.00951e-06, No Iterations 4 T gas min/max = 433, 754.098 DICPCG: Solving for p, Initial residual = 0.930326, Final residual = 0.092552, No Iterations 68 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00301912, global = 4.74693e-08, cumulative = 1.23851e-05 DICPCG: Solving for p, Initial residual = 0.581997, Final residual = 9.74677e-07, No Iterations 158 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 6.26758e-09, global = 5.36448e-14, cumulative = 1.23851e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.00708027, Final residual = 4.78384e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0153872, Final residual = 8.06705e-06, No Iterations 3 Mean pressure:1.35735e+06 Mean temperature:737.986 Mean u':0.297002 ExecutionTime = 3328.27 s ClockTime = 3466 s Courant Number mean: 0.0259762 max: 0.135216 deltaT = 0.000833367 Crank angle = -20.8333 CA-deg deltaZ = 0.000338049 clearance: 0.0142311 Piston speed = 0.405643 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.124791, Final residual = 1.44874e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.139185, Final residual = 1.64475e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0386476, Final residual = 8.34348e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000161458, Final residual = 6.02406e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.174782, Final residual = 1.74883e-06, No Iterations 4 T gas min/max = 433, 759.76 DICPCG: Solving for p, Initial residual = 0.9279, Final residual = 0.0781601, No Iterations 58 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00252369, global = 1.98587e-07, cumulative = 1.25837e-05 DICPCG: Solving for p, Initial residual = 0.512365, Final residual = 9.93535e-07, No Iterations 157 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.93778e-09, global = -5.99699e-14, cumulative = 1.25837e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.00652499, Final residual = 4.12802e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0165835, Final residual = 8.12562e-06, No Iterations 3 Mean pressure:1.39928e+06 Mean temperature:743.144 Mean u':0.295204 ExecutionTime = 3343.14 s ClockTime = 3481 s Courant Number mean: 0.027361 max: 0.137841 deltaT = 0.000833367 Crank angle = -20 CA-deg deltaZ = 0.000325811 clearance: 0.0139053 Piston speed = 0.390958 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.265731, Final residual = 2.46682e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.279752, Final residual = 2.66277e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0316396, Final residual = 5.8297e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000161974, Final residual = 2.09085e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.167554, Final residual = 1.52538e-06, No Iterations 4 T gas min/max = 433, 765.362 DICPCG: Solving for p, Initial residual = 0.927387, Final residual = 0.0795676, No Iterations 69 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00253273, global = 4.80986e-08, cumulative = 1.26318e-05 DICPCG: Solving for p, Initial residual = 0.4979, Final residual = 8.84432e-07, No Iterations 162 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.38601e-09, global = -3.26589e-14, cumulative = 1.26318e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.00593562, Final residual = 3.45935e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0179747, Final residual = 8.20603e-06, No Iterations 3 Mean pressure:1.44184e+06 Mean temperature:748.236 Mean u':0.293266 ExecutionTime = 3359.81 s ClockTime = 3503 s Courant Number mean: 0.026428 max: 0.13194 deltaT = 0.000833367 Crank angle = -19.1667 CA-deg deltaZ = 0.000313452 clearance: 0.0135919 Piston speed = 0.376128 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.162304, Final residual = 1.32843e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.195675, Final residual = 1.48983e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0345968, Final residual = 5.25034e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000163885, Final residual = 8.05973e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.160311, Final residual = 1.31148e-06, No Iterations 4 T gas min/max = 433, 770.894 DICPCG: Solving for p, Initial residual = 0.924133, Final residual = 0.0891442, No Iterations 54 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00279962, global = 1.09429e-07, cumulative = 1.27412e-05 DICPCG: Solving for p, Initial residual = 0.523936, Final residual = 9.27956e-07, No Iterations 162 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.94294e-09, global = 1.78681e-13, cumulative = 1.27412e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.00525249, Final residual = 2.74435e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0192952, Final residual = 8.15203e-06, No Iterations 3 Mean pressure:1.48494e+06 Mean temperature:753.249 Mean u':0.2912 ExecutionTime = 3374.71 s ClockTime = 3518 s Courant Number mean: 0.0270458 max: 0.130747 deltaT = 0.000833367 Crank angle = -18.3333 CA-deg deltaZ = 0.000300977 clearance: 0.0132909 Piston speed = 0.361158 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.171612, Final residual = 1.22833e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.161249, Final residual = 9.9291e-07, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0417914, Final residual = 5.45065e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000161277, Final residual = 5.30791e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.153042, Final residual = 1.12247e-06, No Iterations 4 T gas min/max = 433, 776.344 DICPCG: Solving for p, Initial residual = 0.92057, Final residual = 0.0871084, No Iterations 71 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00269369, global = 3.11135e-08, cumulative = 1.27723e-05 DICPCG: Solving for p, Initial residual = 0.495724, Final residual = 9.7563e-07, No Iterations 161 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 6.27839e-09, global = 5.03603e-14, cumulative = 1.27723e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.00451484, Final residual = 2.07813e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0207629, Final residual = 8.13422e-06, No Iterations 3 Mean pressure:1.52845e+06 Mean temperature:758.172 Mean u':0.288992 ExecutionTime = 3389.73 s ClockTime = 3533 s Courant Number mean: 0.0262668 max: 0.12776 deltaT = 0.000833367 Crank angle = -17.5 CA-deg deltaZ = 0.000288391 clearance: 0.0130025 Piston speed = 0.346055 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.112443, Final residual = 8.10914e-07, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.115905, Final residual = 6.6668e-07, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0361318, Final residual = 4.73825e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000159646, Final residual = 4.99343e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.14575, Final residual = 9.57276e-07, No Iterations 4 T gas min/max = 433, 781.696 DICPCG: Solving for p, Initial residual = 0.916601, Final residual = 0.0718476, No Iterations 69 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00218304, global = 3.72513e-08, cumulative = 1.28096e-05 DICPCG: Solving for p, Initial residual = 0.426196, Final residual = 8.89619e-07, No Iterations 160 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.49315e-09, global = 1.75729e-13, cumulative = 1.28096e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.00372261, Final residual = 1.5888e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.022186, Final residual = 8.00546e-06, No Iterations 3 Mean pressure:1.57223e+06 Mean temperature:762.99 Mean u':0.286653 ExecutionTime = 3404.74 s ClockTime = 3548 s Courant Number mean: 0.0262806 max: 0.128964 deltaT = 0.000833367 Crank angle = -16.6667 CA-deg deltaZ = 0.000275698 clearance: 0.0127268 Piston speed = 0.330824 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.117536, Final residual = 6.40991e-07, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.1437, Final residual = 5.92376e-07, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0400374, Final residual = 4.09954e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000161609, Final residual = 7.94084e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.138429, Final residual = 8.09805e-07, No Iterations 4 T gas min/max = 433, 786.937 DICPCG: Solving for p, Initial residual = 0.914729, Final residual = 0.0843155, No Iterations 71 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00250442, global = 2.6321e-08, cumulative = 1.28359e-05 DICPCG: Solving for p, Initial residual = 0.449344, Final residual = 8.05384e-07, No Iterations 161 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.17479e-09, global = 4.90728e-14, cumulative = 1.28359e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.00315755, Final residual = 1.23927e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0236804, Final residual = 7.85212e-06, No Iterations 3 Mean pressure:1.61614e+06 Mean temperature:767.691 Mean u':0.284177 ExecutionTime = 3419.8 s ClockTime = 3563 s Courant Number mean: 0.0259003 max: 0.127703 deltaT = 0.000833367 Crank angle = -15.8333 CA-deg deltaZ = 0.000262902 clearance: 0.0124639 Piston speed = 0.31547 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.12114, Final residual = 6.57378e-07, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.117944, Final residual = 5.29335e-07, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0457583, Final residual = 4.72292e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.00016262, Final residual = 5.41166e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.131079, Final residual = 6.81243e-07, No Iterations 4 T gas min/max = 433, 792.052 DICPCG: Solving for p, Initial residual = 0.910773, Final residual = 0.0730174, No Iterations 71 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00211847, global = 3.34203e-08, cumulative = 1.28693e-05 DICPCG: Solving for p, Initial residual = 0.403714, Final residual = 8.1354e-07, No Iterations 163 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.18364e-09, global = 1.36529e-13, cumulative = 1.28693e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.00275322, Final residual = 9.87534e-07, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0251631, Final residual = 7.63154e-06, No Iterations 3 Mean pressure:1.66001e+06 Mean temperature:772.261 Mean u':0.281571 ExecutionTime = 3434.81 s ClockTime = 3578 s Courant Number mean: 0.0257387 max: 0.126762 deltaT = 0.000833367 Crank angle = -15 CA-deg deltaZ = 0.00025001 clearance: 0.0122139 Piston speed = 0.3 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.118779, Final residual = 5.1468e-07, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.140873, Final residual = 6.36509e-07, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0459267, Final residual = 3.58278e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000158905, Final residual = 3.44595e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.123698, Final residual = 5.67466e-07, No Iterations 4 T gas min/max = 433, 797.026 DICPCG: Solving for p, Initial residual = 0.906286, Final residual = 0.0877601, No Iterations 72 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00248008, global = 4.26867e-08, cumulative = 1.2912e-05 DICPCG: Solving for p, Initial residual = 0.432124, Final residual = 9.00356e-07, No Iterations 165 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 6.11154e-09, global = -5.54243e-15, cumulative = 1.2912e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.00245938, Final residual = 8.70052e-06, No Iterations 2 DILUPBiCG: Solving for k, Initial residual = 0.0266792, Final residual = 7.39536e-06, No Iterations 3 Mean pressure:1.70364e+06 Mean temperature:776.685 Mean u':0.278835 ExecutionTime = 3451.53 s ClockTime = 3600 s Courant Number mean: 0.0255327 max: 0.125014 deltaT = 0.00100004 Crank angle = -14 CA-deg deltaZ = 0.000282864 clearance: 0.011931 Piston speed = 0.282852 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.167128, Final residual = 1.83029e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.154987, Final residual = 1.60189e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0581343, Final residual = 9.25527e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.00017245, Final residual = 4.21964e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.135357, Final residual = 1.25975e-06, No Iterations 4 T gas min/max = 433, 802.773 DICPCG: Solving for p, Initial residual = 0.886275, Final residual = 0.0775373, No Iterations 78 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00257896, global = 2.01796e-08, cumulative = 1.29322e-05 DICPCG: Solving for p, Initial residual = 0.385184, Final residual = 9.56329e-07, No Iterations 166 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 7.66576e-09, global = 9.78305e-14, cumulative = 1.29322e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.00266033, Final residual = 9.86239e-07, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0333758, Final residual = 1.07827e-06, No Iterations 4 Mean pressure:1.75539e+06 Mean temperature:781.77 Mean u':0.275406 ExecutionTime = 3466.61 s ClockTime = 3615 s Courant Number mean: 0.0302549 max: 0.149307 deltaT = 0.00100004 Crank angle = -13 CA-deg deltaZ = 0.000264015 clearance: 0.011667 Piston speed = 0.264004 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.133117, Final residual = 1.15473e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.169028, Final residual = 1.41313e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.058729, Final residual = 9.39181e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000168924, Final residual = 7.99031e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.125789, Final residual = 1.01124e-06, No Iterations 4 T gas min/max = 433, 808.299 DICPCG: Solving for p, Initial residual = 0.890539, Final residual = 0.0792773, No Iterations 75 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00250455, global = 3.26013e-08, cumulative = 1.29648e-05 DICPCG: Solving for p, Initial residual = 0.346515, Final residual = 8.40024e-07, No Iterations 167 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 7.0607e-09, global = -7.50702e-14, cumulative = 1.29648e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.00337846, Final residual = 9.67123e-07, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0355342, Final residual = 1.00069e-06, No Iterations 4 Mean pressure:1.8062e+06 Mean temperature:786.631 Mean u':0.271806 ExecutionTime = 3481.71 s ClockTime = 3630 s Courant Number mean: 0.0300237 max: 0.145611 deltaT = 0.00100004 Crank angle = -12 CA-deg deltaZ = 0.000245025 clearance: 0.011422 Piston speed = 0.245016 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.180365, Final residual = 1.34574e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.153313, Final residual = 1.0993e-06, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0643016, Final residual = 8.5862e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000166233, Final residual = 7.56295e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.115649, Final residual = 7.95206e-07, No Iterations 4 T gas min/max = 433, 813.556 DICPCG: Solving for p, Initial residual = 0.877601, Final residual = 0.0749761, No Iterations 79 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00227625, global = 1.15145e-08, cumulative = 1.29763e-05 DICPCG: Solving for p, Initial residual = 0.311704, Final residual = 9.00158e-07, No Iterations 164 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 7.9058e-09, global = 1.1719e-13, cumulative = 1.29763e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.00482839, Final residual = 1.73462e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0377431, Final residual = 9.24554e-07, No Iterations 4 Mean pressure:1.85565e+06 Mean temperature:791.221 Mean u':0.268036 ExecutionTime = 3496.8 s ClockTime = 3645 s Courant Number mean: 0.0294295 max: 0.142044 deltaT = 0.00100004 Crank angle = -11 CA-deg deltaZ = 0.000225906 clearance: 0.0111961 Piston speed = 0.225897 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.105543, Final residual = 7.1272e-07, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.129593, Final residual = 8.26141e-07, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0746871, Final residual = 8.01896e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000168948, Final residual = 4.39072e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.105305, Final residual = 6.2013e-07, No Iterations 4 T gas min/max = 433, 818.509 DICPCG: Solving for p, Initial residual = 0.8668, Final residual = 0.0844503, No Iterations 61 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.002438, global = 7.3011e-08, cumulative = 1.30493e-05 DICPCG: Solving for p, Initial residual = 0.315638, Final residual = 8.5557e-07, No Iterations 170 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 7.82664e-09, global = -3.92257e-13, cumulative = 1.30493e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.00686147, Final residual = 2.42956e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0398467, Final residual = 8.37529e-07, No Iterations 4 Mean pressure:1.90327e+06 Mean temperature:795.51 Mean u':0.26412 ExecutionTime = 3511.86 s ClockTime = 3660 s Courant Number mean: 0.0297046 max: 0.142504 deltaT = 0.00100004 Crank angle = -10 CA-deg deltaZ = 0.000206666 clearance: 0.0109894 Piston speed = 0.206657 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.207372, Final residual = 1.03732e-06, No Iterations 4 DILUPBiCG: Solving for Uy, Initial residual = 0.127949, Final residual = 6.93831e-07, No Iterations 4 DILUPBiCG: Solving for Uz, Initial residual = 0.0770743, Final residual = 7.89836e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000166969, Final residual = 4.86017e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0948463, Final residual = 9.83856e-06, No Iterations 3 T gas min/max = 433, 823.129 DICPCG: Solving for p, Initial residual = 0.853495, Final residual = 0.0663259, No Iterations 68 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00180903, global = 3.66509e-08, cumulative = 1.3086e-05 DICPCG: Solving for p, Initial residual = 0.245426, Final residual = 8.99909e-07, No Iterations 170 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 8.04611e-09, global = 6.81027e-13, cumulative = 1.3086e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.00919366, Final residual = 3.03197e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0420756, Final residual = 7.62852e-07, No Iterations 4 Mean pressure:1.94863e+06 Mean temperature:799.468 Mean u':0.260051 ExecutionTime = 3528.47 s ClockTime = 3680 s Courant Number mean: 0.0289696 max: 0.139669 deltaT = 0.000833367 Crank angle = -9.16667 CA-deg deltaZ = 0.000157445 clearance: 0.010832 Piston speed = 0.188926 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.108864, Final residual = 5.33231e-06, No Iterations 3 DILUPBiCG: Solving for Uy, Initial residual = 0.109795, Final residual = 5.7234e-06, No Iterations 3 DILUPBiCG: Solving for Uz, Initial residual = 0.0739547, Final residual = 3.3966e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000150502, Final residual = 6.28295e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0720356, Final residual = 3.30876e-06, No Iterations 3 T gas min/max = 433, 826.694 DICPCG: Solving for p, Initial residual = 0.860583, Final residual = 0.070798, No Iterations 59 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00148061, global = 6.31596e-08, cumulative = 1.31491e-05 DICPCG: Solving for p, Initial residual = 0.233024, Final residual = 9.98668e-07, No Iterations 165 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 7.39221e-09, global = -2.12025e-13, cumulative = 1.31491e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.010324, Final residual = 1.68212e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0374261, Final residual = 4.94192e-06, No Iterations 3 Mean pressure:1.98435e+06 Mean temperature:802.484 Mean u':0.256539 ExecutionTime = 3676.21 s ClockTime = 3827 s Courant Number mean: 0.0243442 max: 0.114456 deltaT = 0.000833367 Crank angle = -8.33333 CA-deg deltaZ = 0.000143949 clearance: 0.010688 Piston speed = 0.172732 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.109189, Final residual = 4.25578e-06, No Iterations 3 DILUPBiCG: Solving for Uy, Initial residual = 0.159251, Final residual = 6.2631e-06, No Iterations 3 DILUPBiCG: Solving for Uz, Initial residual = 0.087723, Final residual = 3.44683e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000151407, Final residual = 2.44663e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0636146, Final residual = 2.57315e-06, No Iterations 3 T gas min/max = 433, 829.952 DICPCG: Solving for p, Initial residual = 0.831826, Final residual = 0.0799744, No Iterations 76 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00159423, global = 1.20717e-08, cumulative = 1.31612e-05 DICPCG: Solving for p, Initial residual = 0.248374, Final residual = 9.16754e-07, No Iterations 169 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 6.79212e-09, global = 5.43754e-13, cumulative = 1.31612e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.0121713, Final residual = 1.77565e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0389696, Final residual = 4.57603e-06, No Iterations 3 Mean pressure:2.01781e+06 Mean temperature:805.199 Mean u':0.252937 ExecutionTime = 3790.73 s ClockTime = 3942 s Courant Number mean: 0.0237458 max: 0.112947 deltaT = 0.000833367 Crank angle = -7.5 CA-deg deltaZ = 0.0001304 clearance: 0.0105576 Piston speed = 0.156474 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0459523, Final residual = 2.1522e-06, No Iterations 3 DILUPBiCG: Solving for Uy, Initial residual = 0.0525447, Final residual = 1.69517e-06, No Iterations 3 DILUPBiCG: Solving for Uz, Initial residual = 0.0898153, Final residual = 3.05213e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000148241, Final residual = 1.16907e-06, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0557389, Final residual = 1.99668e-06, No Iterations 3 T gas min/max = 433, 832.909 DICPCG: Solving for p, Initial residual = 0.820594, Final residual = 0.0781468, No Iterations 64 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00144083, global = 6.89461e-08, cumulative = 1.32301e-05 DICPCG: Solving for p, Initial residual = 0.224251, Final residual = 8.30606e-07, No Iterations 169 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 6.0921e-09, global = 2.69516e-13, cumulative = 1.32301e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.0141611, Final residual = 1.83698e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0404139, Final residual = 4.19028e-06, No Iterations 3 Mean pressure:2.0488e+06 Mean temperature:807.622 Mean u':0.249261 ExecutionTime = 3905.22 s ClockTime = 4057 s Courant Number mean: 0.0238816 max: 0.11188 deltaT = 0.000833367 Crank angle = -6.66667 CA-deg deltaZ = 0.000116803 clearance: 0.0104408 Piston speed = 0.140158 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.114612, Final residual = 3.72922e-06, No Iterations 3 DILUPBiCG: Solving for Uy, Initial residual = 0.139591, Final residual = 4.37067e-06, No Iterations 3 DILUPBiCG: Solving for Uz, Initial residual = 0.0966616, Final residual = 2.95999e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000147529, Final residual = 6.44453e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0479858, Final residual = 1.52198e-06, No Iterations 3 T gas min/max = 433, 835.558 DICPCG: Solving for p, Initial residual = 0.797084, Final residual = 0.0667352, No Iterations 78 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00114051, global = 7.11166e-09, cumulative = 1.32372e-05 DICPCG: Solving for p, Initial residual = 0.183808, Final residual = 8.70658e-07, No Iterations 167 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 6.26833e-09, global = 1.28109e-12, cumulative = 1.32372e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.0162951, Final residual = 1.87641e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0419072, Final residual = 3.84258e-06, No Iterations 3 Mean pressure:2.0771e+06 Mean temperature:809.747 Mean u':0.245511 ExecutionTime = 4019.92 s ClockTime = 4171 s Courant Number mean: 0.0232816 max: 0.110304 deltaT = 0.000833367 Crank angle = -5.83333 CA-deg deltaZ = 0.000103163 clearance: 0.0103377 Piston speed = 0.123791 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0362548, Final residual = 1.19212e-06, No Iterations 3 DILUPBiCG: Solving for Uy, Initial residual = 0.0396227, Final residual = 1.14655e-06, No Iterations 3 DILUPBiCG: Solving for Uz, Initial residual = 0.104079, Final residual = 2.8476e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000144917, Final residual = 8.00572e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0402587, Final residual = 1.14782e-06, No Iterations 3 T gas min/max = 433, 837.884 DICPCG: Solving for p, Initial residual = 0.755406, Final residual = 0.0702651, No Iterations 63 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00112154, global = 4.10204e-08, cumulative = 1.32783e-05 DICPCG: Solving for p, Initial residual = 0.177337, Final residual = 7.88438e-07, No Iterations 167 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.69185e-09, global = 1.84206e-13, cumulative = 1.32783e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.0185524, Final residual = 1.88581e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0432939, Final residual = 3.48864e-06, No Iterations 3 Mean pressure:2.10245e+06 Mean temperature:811.56 Mean u':0.241702 ExecutionTime = 4134.61 s ClockTime = 4286 s Courant Number mean: 0.0232709 max: 0.108693 deltaT = 0.000833367 Crank angle = -5 CA-deg deltaZ = 8.94852e-05 clearance: 0.0102482 Piston speed = 0.107378 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0882024, Final residual = 2.01323e-06, No Iterations 3 DILUPBiCG: Solving for Uy, Initial residual = 0.0860071, Final residual = 2.00302e-06, No Iterations 3 DILUPBiCG: Solving for Uz, Initial residual = 0.11703, Final residual = 2.57628e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000144908, Final residual = 9.3352e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0325476, Final residual = 8.24292e-07, No Iterations 3 T gas min/max = 433, 839.876 DICPCG: Solving for p, Initial residual = 0.704346, Final residual = 0.0495395, No Iterations 79 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000734179, global = 3.49448e-09, cumulative = 1.32818e-05 DICPCG: Solving for p, Initial residual = 0.116935, Final residual = 8.99409e-07, No Iterations 166 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 6.4435e-09, global = 2.01188e-12, cumulative = 1.32818e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.0209542, Final residual = 1.8737e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0446975, Final residual = 3.16289e-06, No Iterations 3 Mean pressure:2.12463e+06 Mean temperature:813.051 Mean u':0.237837 ExecutionTime = 4251.27 s ClockTime = 4412 s Courant Number mean: 0.0227028 max: 0.106833 deltaT = 0.00100004 Crank angle = -4 CA-deg deltaZ = 8.92812e-05 clearance: 0.0101589 Piston speed = 0.0892776 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0342753, Final residual = 1.51121e-06, No Iterations 3 DILUPBiCG: Solving for Uy, Initial residual = 0.034207, Final residual = 1.46133e-06, No Iterations 3 DILUPBiCG: Solving for Uz, Initial residual = 0.161247, Final residual = 6.64808e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000156765, Final residual = 6.39009e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0293702, Final residual = 1.26346e-06, No Iterations 3 T gas min/max = 433, 841.84 DICPCG: Solving for p, Initial residual = 0.611289, Final residual = 0.0604225, No Iterations 73 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.00102347, global = 2.9354e-08, cumulative = 1.33111e-05 DICPCG: Solving for p, Initial residual = 0.132103, Final residual = 9.57442e-07, No Iterations 168 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 8.56874e-09, global = 1.1764e-13, cumulative = 1.33111e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.0270127, Final residual = 4.0314e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0542245, Final residual = 6.42335e-06, No Iterations 3 Mean pressure:2.14686e+06 Mean temperature:814.436 Mean u':0.233178 ExecutionTime = 4386.63 s ClockTime = 4548 s Courant Number mean: 0.0268985 max: 0.124779 deltaT = 0.00100004 Crank angle = -3 CA-deg deltaZ = 6.94901e-05 clearance: 0.0100894 Piston speed = 0.0694873 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0787604, Final residual = 2.91478e-06, No Iterations 3 DILUPBiCG: Solving for Uy, Initial residual = 0.0772132, Final residual = 2.85816e-06, No Iterations 3 DILUPBiCG: Solving for Uz, Initial residual = 0.17225, Final residual = 5.65825e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000152979, Final residual = 2.47052e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0203877, Final residual = 7.37989e-07, No Iterations 3 T gas min/max = 433, 843.344 DICPCG: Solving for p, Initial residual = 0.526469, Final residual = 0.0448807, No Iterations 81 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000677636, global = 5.12609e-09, cumulative = 1.33162e-05 DICPCG: Solving for p, Initial residual = 0.0850074, Final residual = 8.20017e-07, No Iterations 172 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 7.74723e-09, global = 6.37179e-13, cumulative = 1.33162e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.0308897, Final residual = 3.9682e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0560356, Final residual = 5.69074e-06, No Iterations 3 Mean pressure:2.16406e+06 Mean temperature:815.381 Mean u':0.228469 ExecutionTime = 4521.98 s ClockTime = 4683 s Courant Number mean: 0.0261913 max: 0.122241 deltaT = 0.00100004 Crank angle = -2 CA-deg deltaZ = 4.96621e-05 clearance: 0.0100397 Piston speed = 0.0496602 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.034164, Final residual = 9.28931e-07, No Iterations 3 DILUPBiCG: Solving for Uy, Initial residual = 0.0335434, Final residual = 9.77324e-07, No Iterations 3 DILUPBiCG: Solving for Uz, Initial residual = 0.221984, Final residual = 6.38323e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000149547, Final residual = 1.53341e-07, No Iterations 2 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0138562, Final residual = 4.03942e-07, No Iterations 3 T gas min/max = 433, 844.332 DICPCG: Solving for p, Initial residual = 0.400955, Final residual = 0.0382912, No Iterations 68 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000519381, global = 2.58014e-08, cumulative = 1.3342e-05 DICPCG: Solving for p, Initial residual = 0.0619232, Final residual = 9.79687e-07, No Iterations 166 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 9.54357e-09, global = -1.40521e-13, cumulative = 1.3342e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.0349474, Final residual = 3.82441e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0576986, Final residual = 4.993e-06, No Iterations 3 Mean pressure:2.17588e+06 Mean temperature:815.837 Mean u':0.22373 ExecutionTime = 4657.4 s ClockTime = 4819 s Courant Number mean: 0.0258267 max: 0.119391 deltaT = 0.00100004 Crank angle = -1 CA-deg deltaZ = 2.98078e-05 clearance: 0.0100099 Piston speed = 0.0298066 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.058919, Final residual = 1.4056e-06, No Iterations 3 DILUPBiCG: Solving for Uy, Initial residual = 0.0521199, Final residual = 1.21078e-06, No Iterations 3 DILUPBiCG: Solving for Uz, Initial residual = 0.26167, Final residual = 6.43433e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000147142, Final residual = 4.39491e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.00888936, Final residual = 4.73904e-06, No Iterations 2 T gas min/max = 433, 844.783 DICPCG: Solving for p, Initial residual = 0.240436, Final residual = 0.0214958, No Iterations 82 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000256511, global = 2.92608e-09, cumulative = 1.3345e-05 DICPCG: Solving for p, Initial residual = 0.0309584, Final residual = 9.10469e-07, No Iterations 165 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 9.11656e-09, global = 2.29161e-12, cumulative = 1.3345e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.0392389, Final residual = 3.63961e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0592878, Final residual = 4.36079e-06, No Iterations 3 Mean pressure:2.18212e+06 Mean temperature:815.781 Mean u':0.218973 ExecutionTime = 4792.81 s ClockTime = 4954 s Courant Number mean: 0.0251016 max: 0.116061 deltaT = 0.00100004 Crank angle = -2.77545e-14 CA-deg deltaZ = 9.9377e-06 clearance: 0.01 Piston speed = 0.00993731 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0213264, Final residual = 4.14364e-07, No Iterations 3 DILUPBiCG: Solving for Uy, Initial residual = 0.0207935, Final residual = 4.6749e-07, No Iterations 3 DILUPBiCG: Solving for Uz, Initial residual = 0.308155, Final residual = 6.26076e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000146126, Final residual = 3.77926e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0120374, Final residual = 8.68253e-06, No Iterations 2 T gas min/max = 433, 844.685 DICPCG: Solving for p, Initial residual = 0.0448551, Final residual = 0.004431, No Iterations 87 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 4.55319e-05, global = 1.57276e-09, cumulative = 1.33465e-05 DICPCG: Solving for p, Initial residual = 0.0085356, Final residual = 7.81685e-07, No Iterations 87 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 7.97871e-09, global = 1.01283e-09, cumulative = 1.33476e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.0437656, Final residual = 3.42435e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0607473, Final residual = 3.78066e-06, No Iterations 3 Mean pressure:2.18265e+06 Mean temperature:815.205 Mean u':0.214213 ExecutionTime = 4929.37 s ClockTime = 5092 s Courant Number mean: 0.0243786 max: 0.111817 deltaT = 0.000833367 Crank angle = 0.833333 CA-deg deltaZ = -6.90128e-06 clearance: 0.0100069 Piston speed = -0.0082812 m/s Solving cloud sprayCloud Cloud: sprayCloud Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 Rotational kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 D10, D32, Dmax (mu) = 0, 0, 0 Liquid penetration 95% mass (m) = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for Ux, Initial residual = 0.0146477, Final residual = 3.19123e-06, No Iterations 2 DILUPBiCG: Solving for Uy, Initial residual = 0.013636, Final residual = 2.82048e-06, No Iterations 2 DILUPBiCG: Solving for Uz, Initial residual = 0.298747, Final residual = 2.34869e-06, No Iterations 3 DILUPBiCG: Solving for C7H16, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for O2, Initial residual = 0.000129427, Final residual = 5.47599e-06, No Iterations 1 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.0188619, Final residual = 5.08086e-06, No Iterations 2 T gas min/max = 433, 844.142 DICPCG: Solving for p, Initial residual = 0.241275, Final residual = 0.0204481, No Iterations 67 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0.000165946, global = -6.14907e-09, cumulative = 1.33414e-05 DICPCG: Solving for p, Initial residual = 0.0246153, Final residual = 9.9418e-07, No Iterations 157 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 8.30557e-09, global = -1.01264e-12, cumulative = 1.33414e-05 DILUPBiCG: Solving for epsilon, Initial residual = 0.041855, Final residual = 1.38653e-06, No Iterations 3 DILUPBiCG: Solving for k, Initial residual = 0.0526694, Final residual = 1.39362e-06, No Iterations 3 Mean pressure:2.17861e+06 Mean temperature:814.286 Mean u':0.210228 ExecutionTime = 5044.49 s ClockTime = 5208 s Courant Number mean: 0.0196981 max: 0.0896376 deltaT = 0.000833367 Crank angle = 1.66667 CA-deg deltaZ = -2.07013e-05 clearance: 0.0100276 Piston speed = -0.0248405 m/s Solving cloud sprayCloud --> FOAM FATAL ERROR: Integrating outside table 0..0.0125005 not implemented. t1:0.0118338 t2:0.0126672 From function linearInterpolationWeights::integrationWeights(..) in file interpolations/interpolationWeights/linearInterpolationWeights/linearInterpolationWeights.C at line 180. FOAM exiting