/*---------------------------------------------------------------------------*\ | ========= | | | \\ / F ield | OpenFOAM: The Open Source CFD Toolbox | | \\ / O peration | Version: 3.0.x | | \\ / A nd | Web: www.OpenFOAM.org | | \\/ M anipulation | | \*---------------------------------------------------------------------------*/ Build : 3.0.x-1c517d6c8485 Exec : reactingParcelFilmFoam Date : Aug 03 2016 Time : 12:03:31 Host : "MACHINE" PID : 1018 Case : /home/ofuser/OpenFOAM/ofuser-3.0.x/run/tutorials/lagrangian/reactingParcelFilmFoam/hotBoxes 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 time Create mesh for time = 0 PIMPLE: Operating solver in PISO mode Creating combustion model Selecting combustion model PaSR Selecting chemistry type { chemistrySolver noChemistrySolver; chemistryThermo psi; } Selecting thermodynamics package { type hePsiThermo; mixture reactingMixture; transport sutherland; thermo janaf; energy sensibleEnthalpy; equationOfState perfectGas; specie specie; } Selecting chemistryReader foamChemistryReader chemistryModel: Number of species = 3 and reactions = 0 using integrated reaction rate Creating component thermo properties: multi-component carrier - 3 species liquids - 1 components solids - 0 components Creating field rho Reading field U Reading/calculating face flux field phi Creating turbulence model Selecting turbulence model type RAS Selecting RAS turbulence model kEpsilon Creating field dpdt Creating field kinetic energy K Reading g Reading hRef Calculating field g.h No MRF models present No finite volume options present Constructing reacting cloud Constructing particle forces Selecting particle force sphereDrag Selecting particle force gravity Constructing cloud functions none Constructing particle injection models Creating injector: model1 Selecting injection model coneInjection Constructing 3-D injection Selecting distribution model RosinRammler Selecting dispersion model none Selecting patch interaction model standardWallInteraction Selecting stochastic collision model none Selecting surface film model thermoSurfaceFilm Applying splashBai interaction model Selecting U integration scheme Euler Selecting heat transfer model none Selecting T integration scheme analytical Selecting composition model singlePhaseMixture Selecting phase change model none Selecting radiationModel none Constructing surface film model Selecting surfaceFilmModel thermoSingleLayer Selecting region model functions none Selecting filmThermoModel liquid Selecting film injection models curvatureSeparation drippingInjection Selecting distribution model RosinRammler Selecting filmTurbulenceModel laminar Selecting film force models thermocapillary contactAngle Selecting distribution model normal Selecting filmViscosityModel liquid Selecting heatTransferModel mappedConvectiveHeatTransfer Selecting heatTransferModel constant Selecting phaseChangeModel standardPhaseChange Selecting radiationModel none Courant Number mean: 0 max: 0 Starting time loop Courant Number mean: 0 max: 0 Film max Courant number: 0 deltaT = 0.0001436781609 Time = 0.000143678 Solving 3-D cloud reactingCloud1 Cloud: reactingCloud1 Current number of parcels = 0 Current mass in system = 0 Linear momentum = (0 0 0) |Linear momentum| = 0 Linear kinetic energy = 0 model1: number of parcels added = 0 mass introduced = 0 Parcels absorbed into film = 0 New film detached parcels = 0 New film splash parcels = 0 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 0, 0 Mass transfer phase change = 0 Evolving thermoSingleLayer for region wallFilmRegion diagonal: Solving for deltaf*rhof, Initial residual = 0, Final residual = 0, No Iterations 0 smoothSolver: Solving for Ufx, Initial residual = 0.9912919068, Final residual = 1.793914086e-17, No Iterations 1 smoothSolver: Solving for Ufy, Initial residual = 0.9904653317, Final residual = 1.986328704e-17, No Iterations 1 smoothSolver: Solving for Ufz, Initial residual = 0.9973363737, Final residual = 1.832228392e-17, No Iterations 1 smoothSolver: Solving for hf, Initial residual = 1, Final residual = 2.147073609e-19, No Iterations 1 smoothSolver: Solving for deltaf, Initial residual = 0, Final residual = 0, No Iterations 0 diagonal: Solving for deltaf*rhof, Initial residual = 0, Final residual = 0, No Iterations 0 Surface film: thermoSingleLayer added mass = 0 current mass = 0 min/max(mag(U)) = 0, 3.286543803e-19 min/max(delta) = 0, 0 coverage = 0 injected mass = 0 - patch: region0_to_wallFilmRegion_cubeFaces: 0 - patch: region0_to_wallFilmRegion_floorFaces: 0 min/max(T) = 350, 350 mass phase change = 0 vapourisation rate = 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 PIMPLE: iteration 1 DILUPBiCG: Solving for Ux, Initial residual = 0.999999712, Final residual = 3.010989382e-08, No Iterations 1 DILUPBiCG: Solving for Uy, Initial residual = 0.9999997108, Final residual = 3.029125941e-08, No Iterations 1 DILUPBiCG: Solving for Uz, Initial residual = 1, Final residual = 2.330758672e-09, No Iterations 1 DILUPBiCG: Solving for O2, Initial residual = 4.387856388e-05, Final residual = 6.517973815e-13, No Iterations 1 DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 0.9851987882, Final residual = 2.632412106e-09, No Iterations 1 T gas min/max = 300, 300 GAMG: Solving for p_rgh, Initial residual = 0.003766716202, Final residual = 0.0002246622946, No Iterations 2 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.908922321e-08, global = -1.507838335e-11, cumulative = -1.507838335e-11 GAMG: Solving for p_rgh, Initial residual = 0.000224389993, Final residual = 4.088294108e-07, No Iterations 4 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.462471344e-11, global = -2.39657082e-14, cumulative = -1.510234906e-11 DILUPBiCG: Solving for epsilon, Initial residual = 2.192778492e-05, Final residual = 3.229385387e-13, No Iterations 1 DILUPBiCG: Solving for k, Initial residual = 0.9999989758, Final residual = 2.977799646e-08, No Iterations 1 ExecutionTime = 27.89 s ClockTime = 28 s