Create time Create mesh for time = 0 Selecting fvMeshDistributor loadBalancer Selecting distributor zoltan Selecting solver multicomponentFluid Selecting thermodynamics package { type hePsiThermo; mixture multiComponentMixture; transport sutherland; thermo janaf; energy sensibleEnthalpy; equationOfState perfectGas; specie specie; } Selecting turbulence model type laminar Selecting laminar stress model Stokes No MRF models present Courant Number mean: 2.73409e-05 max: 0.000175681 Selecting combustion model laminar Selecting chemistry solver { solver ode; method chemistryModel; } odeChemistryModel: Number of species = 5 chemistryModel: Number of species = 5 and reactions = 1 Selecting ODE solver seulex using integrated reaction rate Selecting thermophysical transport type laminar Selecting default laminar thermophysical transport model unityLewisFourier PIMPLE: No convergence criteria found PIMPLE: Operating solver in transient mode with 1 outer corrector PIMPLE: Operating solver in PISO mode Starting time loop Courant Number mean: 2.73409e-05 max: 0.000175681 deltaT = 1.11111e-06 Time = 1.11111e-06s diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCGStab: Solving for O2, Initial residual = 1, Final residual = 1.26231e-10, No Iterations 1 DILUPBiCGStab: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCGStab: Solving for CH4, Initial residual = 1, Final residual = 1.26283e-10, No Iterations 1 DILUPBiCGStab: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCGStab: Solving for h, Initial residual = 1, Final residual = 1.2625e-10, No Iterations 1 DICPCG: Solving for p, Initial residual = 1, Final residual = 0.0291404, No Iterations 1 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 1.242e-06, global = -6.6435e-07, cumulative = -6.6435e-07 DICPCG: Solving for p, Initial residual = 0.00828587, Final residual = 3.63402e-07, No Iterations 4 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 5.44339e-11, global = -2.80532e-11, cumulative = -6.64378e-07 ExecutionTime = 0.097289 s ClockTime = 0 s Courant Number mean: 3.71025e-05 max: 0.000195819 deltaT = 1.26984e-06 Time = 2.38095e-06s diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCGStab: Solving for O2, Initial residual = 0.240887, Final residual = 4.03063e-11, No Iterations 1 DILUPBiCGStab: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCGStab: Solving for CH4, Initial residual = 0.240844, Final residual = 4.0334e-11, No Iterations 1 DILUPBiCGStab: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCGStab: Solving for h, Initial residual = 0.296454, Final residual = 1.4082e-10, No Iterations 1 DICPCG: Solving for p, Initial residual = 0.300101, Final residual = 0.0178395, No Iterations 1 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.55422e-06, global = -2.44847e-06, cumulative = -3.11285e-06 DICPCG: Solving for p, Initial residual = 0.0114237, Final residual = 1.12274e-07, No Iterations 5 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 3.48946e-11, global = -1.97666e-11, cumulative = -3.11287e-06 ExecutionTime = 0.099346 s ClockTime = 0 s Courant Number mean: 6.06108e-05 max: 0.000225148 [3] imbalance 0.000257 0.010254 0.010511 0.0105128 [1] imbalance 0.000277 0.010254 0.010531 0.0105128 [2] imbalance 0.000248 0.010254 0.010502 0.0105128 [0] imbalance 0.000253 0.010254 0.010507 0.0105128 Redistributing mesh with imbalance 0.00173599 deltaT = 1.52381e-06 Time = 3.90476e-06s diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 [3] #0 Foam::error::printStack(Foam::Ostream&)[0] #0 Foam::error::printStack(Foam::Ostream&)[1] #0 Foam::error::printStack(Foam::Ostream&)[2] #0 Foam::error::printStack(Foam::Ostream&) at ??:? at ??:? at ??:? at ??:? [1] #1 Foam::sigFpe::sigHandler(int)[2] #1 Foam::sigFpe::sigHandler(int)[3] #1 Foam::sigFpe::sigHandler(int)[0] #1 Foam::sigFpe::sigHandler(int) at ??:? [1] #2 ? at ??:? [2] #2 ? at ??:? [3] #2 ? in "/lib/x86_64-linux-gnu/libc.so.6" in "/lib/x86_64-linux-gnu/libc.so.6" [2] #3 [1] #3 Foam::divide(Foam::Field&, Foam::UList const&, Foam::UList const&)Foam::divide(Foam::Field&, Foam::UList const&, Foam::UList const&) at ??:? [0] #2 ? in "/lib/x86_64-linux-gnu/libc.so.6" [3] #3 Foam::divide(Foam::Field&, Foam::UList const&, Foam::UList const&) in "/lib/x86_64-linux-gnu/libc.so.6" [0] #3 Foam::divide(Foam::Field&, Foam::UList const&, Foam::UList const&) at ??:? at ??:? [3] #4 [2] #4 Foam::tmp > Foam::operator/(Foam::tmp > const&, Foam::tmp > const&)Foam::tmp > Foam::operator/(Foam::tmp > const&, Foam::tmp > const&) at ??:? [1] #4 Foam::tmp > Foam::operator/(Foam::tmp > const&, Foam::tmp > const&) at ??:? at ??:? at ??:? [3] #5 Foam::fluidThermo::nu() const[2] #5 Foam::fluidThermo::nu() const[1] #5 Foam::fluidThermo::nu() const at ??:? [0] #4 Foam::tmp > Foam::operator/(Foam::tmp > const&, Foam::tmp > const&) at ??:? [0] #5 Foam::fluidThermo::nu() const at ??:? [2] #6 Foam::laminarModels::Stokes::nuEff() const at ??:? at ??:? [1] #[3] #6 Foam::laminarModels::Stokes::nuEff() const6 Foam::laminarModels::Stokes::nuEff() const at ??:? [0] #6 Foam::laminarModels::Stokes::nuEff() const at ??:? at ??:? at ??:? at ??:? [3] #7 [1] #7 [0] #7 Foam::linearViscousStress >::divDevTau(Foam::GeometricField, Foam::fvPatchField, Foam::volMesh>&) constFoam::linearViscousStress >::divDevTau(Foam::GeometricField, Foam::fvPatchField, Foam::volMesh>&) constFoam::linearViscousStress >::divDevTau(Foam::GeometricField, Foam::fvPatchField, Foam::volMesh>&) const[2] #7 Foam::linearViscousStress >::divDevTau(Foam::GeometricField, Foam::fvPatchField, Foam::volMesh>&) const at ??:? [0] #8 Foam::solvers::isothermalFluid::momentumPredictor() at ??:? [3] #8 Foam::solvers::isothermalFluid::momentumPredictor() at ??:? [1] #8 Foam::solvers::isothermalFluid::momentumPredictor() at ??:? [2] #8 Foam::solvers::isothermalFluid::momentumPredictor() at ??:? [0] #9 at ??:? [3] #9 at ??:? [1] #9 at ??:? ... Floating point exception Floating point exception Floating point exception -------------------------------------------------------------------------- Primary job terminated normally, but 1 process returned a non-zero exit code. Per user-direction, the job has been aborted. -------------------------------------------------------------------------- Floating point exception -------------------------------------------------------------------------- mpirun detected that one or more processes exited with non-zero status, thus causing the job to be terminated. The first process to do so was: Process name: [[8152,1],1] Exit code: 136