reactingFoam running error
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I tried to set up the Tutorial Eleven reacting foam found http://www.cfd.at/downloads/2014_OFoam_Tut_Complete.pdf
I got the error as below. Can someone help me? /*---------------------------------------------------------------------------*\ | ========= | | | \\ / F ield | OpenFOAM: The Open Source CFD Toolbox | | \\ / O peration | Version: v1612+ | | \\ / A nd | Web: www.OpenFOAM.com | | \\/ M anipulation | | \*---------------------------------------------------------------------------*/ Build : v1612+ Exec : reactingFoam Date : Jan 17 2017 Time : 16:47:09 Host : "belledonne" PID : 6002 Case : /home/gao/OpenFOAM/gao-v1612+/run/counterFlowFlame2D_v2 nProcs : 1 sigFpe : Enabling floating point exception trapping (FOAM_SIGFPE). fileModificationChecking : Monitoring run-time modified files using timeStampMaster (fileModificationSkew 10) allowSystemOperations : Allowing user-supplied system call operations // * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * // Create time Create mesh for time = 0 PIMPLE: Operating solver in PISO mode Creating reaction model Selecting combustion model laminar<psiChemistryCombustion> Selecting chemistry type { chemistrySolver EulerImplicit; chemistryThermo psi; } Selecting thermodynamics package { type hePsiThermo; mixture reactingMixture; transport sutherland; thermo janaf; energy sensibleEnthalpy; equationOfState perfectGas; specie specie; } Selecting chemistryReader foamChemistryReader elements not defined in "/home/gao/OpenFOAM/gao-v1612+/run/counterFlowFlame2D_v2/constant/reactions" chemistryModel: Number of species = 5 and reactions = 1 using integrated reaction rate Reading field U Reading/calculating face flux field phi Creating turbulence model. Selecting turbulence model type laminar Selecting laminar stress model Stokes Creating field dpdt Creating field kinetic energy K No MRF models present No finite volume options present Courant Number mean: 2.99581e-08 max: 1.72209e-05 Starting time loop Courant Number mean: 2.99581e-08 max: 1.72209e-05 deltaT = 1.2e-06 Time = 1.2e-06 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 PIMPLE: iteration 1 #0 Foam::error::printStack(Foam::Ostream&) at ??:? #1 Foam::sigFpe::sigHandler(int) at ??:? #2 ? in "/lib/x86_64-linux-gnu/libc.so.6" #3 Foam::divide(Foam::Field<double>&, Foam::UList<double> const&, Foam::UList<double> const&) at ??:? #4 Foam::tmp<Foam::GeometricField<double, Foam::fvPatchField, Foam::volMesh> > Foam::operator/<Foam::fvPatchField, Foam::volMesh>(Foam::tmp<Foam::GeometricField<doub le, Foam::fvPatchField, Foam::volMesh> > const&, Foam::tmp<Foam::GeometricField<double, Foam::fvPatchField, Foam::volMesh> > const&) at ??:? #5 Foam::fluidThermo::nu() const at ??:? #6 Foam::laminarModels::Stokes<Foam::ThermalDiffusivi ty<Foam::CompressibleTurbulenceModel<Foam::fluidTh ermo> > >::nuEff() const at ??:? #7 Foam::linearViscousStress<Foam::laminarModel<Foam: :ThermalDiffusivity<Foam::CompressibleTurbulenceMo del<Foam::fluidThermo> > > >::divDevRhoReff(Foam::GeometricField<Foam::Vector <double>, Foam::fvPatchField, Foam::volMesh>&) const at ??:? #8 ? at ??:? #9 __libc_start_main in "/lib/x86_64-linux-gnu/libc.so.6" #10 ? at ??:? Exception en point flottant (core dumped) |
The tutorial is prepared with OF 2.3.0
So I run this case with my old version OF 2.4.0 with three small adaptions, the case starts running. So I am wondering when did OF introduce some bugs here? Can someone help me to fix the bug? I am new to OF. Quote:
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reactingFoam solver errors
Hi all,
As a openFoam beginner, I've run a simulation in reactingFoam and unfortunately I just got these codes with No iteration ! Is there anyone who would help me please? . . . Time = 2.46472e-05 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 PIMPLE: iteration 1 DILUPBiCG: Solving for O2, 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 CH4, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 7.83352e-07, Final residual = 7.83352e-07, No Iterations 0 min/max(T) = 358.241, 1499.98 DICPCG: Solving for p, Initial residual = 5.76649e-07, Final residual = 5.76649e-07, No Iterations 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 7.65015e-07, global = -2.09684e-17, cumulative = -0.00201457 rho max/min : 2.50857 2.33323e-06 DICPCG: Solving for p, Initial residual = 5.76649e-07, Final residual = 5.76649e-07, No Iterations 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 7.65015e-07, global = -2.08342e-17, cumulative = -0.00201457 rho max/min : 2.50857 2.33323e-06 ExecutionTime = 118.72 s ClockTime = 120 s Courant Number mean: 6.95254e-05 max: 0.399999 deltaT = 9.51118e-12 Time = 2.46472e-05 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 PIMPLE: iteration 1 DILUPBiCG: Solving for O2, 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 CH4, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCG: Solving for h, Initial residual = 7.83341e-07, Final residual = 7.83341e-07, No Iterations 0 min/max(T) = 358.241, 1499.98 DICPCG: Solving for p, Initial residual = 5.76649e-07, Final residual = 5.76649e-07, No Iterations 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 7.65015e-07, global = 3.51658e-18, cumulative = -0.00201457 rho max/min : 2.50857 2.33323e-06 DICPCG: Solving for p, Initial residual = 5.76649e-07, Final residual = 5.76649e-07, No Iterations 0 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 7.65015e-07, global = 3.58657e-18, cumulative = -0.00201457 rho max/min : 2.50857 2.33323e-06 ExecutionTime = 118.77 s ClockTime = 120 s Courant Number mean: 6.95254e-05 max: 0.399999 deltaT = 9.51119e-12 . . . |
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