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SigFpe error with ReitzKHRT and primary atomization models |
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August 9, 2018, 08:04 |
SigFpe error with ReitzKHRT and primary atomization models
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New Member
Shailja
Join Date: Nov 2017
Posts: 16
Rep Power: 9 |
Hii
I have compiled a new liquid named myC7H16 in user directory and it is running well with no atomization model and ReitzDiwakar model. however As soon as i try to change from no atomization to LISA model or any other Model (e.g ReitzKHRT) in place of secondary atomization model, it crashes with following error: Create time Create mesh for time = 0 PIMPLE: Operating solver in PISO mode Reading g .................................................. .................... .................................................. .................... .................................................. .................... Participating liquid species: myC7H16 Selecting AtomizationModel none Selecting BreakupModel ReitzKHRT Average parcel mass: 2.4e-10 Selecting radiationModel none No finite volume options present Courant Number mean: 0 max: 0 Starting time loop Courant Number mean: 0 max: 0 deltaT = 2.94118e-06 Time = 2.94118e-06 Solving 3-D cloud sprayCloud #0 Foam::error:rintStack(Foam::Ostream&) at ??:? #1 Foam::sigFpe::sigHandler(int) at ??:? #2 ? in "/lib/x86_64-linux-gnu/libc.so.6" #3 Foam::ReitzKHRT<Foam::SprayCloud<Foam::ReactingClo ud<Foam::ThermoCloud<Foam::KinematicCloud<Foam::Cl oud<Foam::SprayParcel<Foam::ReactingParcel<Foam::T hermoParcel<Foam::KinematicParcel<Foam:article> > > > > > > > > >::update(double, Foam::Vector<double> const&, double&, double&, double&, double&, double&, double&, double&, double, double, double, double, Foam::Vector<double> const&, double, double, Foam::Vector<double> const&, double, double, double&, double&) at ??:? #4 ? at ??:? #5 ? at ??:? #6 ? at ??:? #7 ? at ??:? #8 ? at ??:? #9 ? at ??:? #10 ? at ??:? #11 ? at ??:? #12 __libc_start_main in "/lib/x86_64-linux-gnu/libc.so.6" #13 ? at ??:? Floating point exception (core dumped) I do not understand this as the same liquid is running well with ReitzDiwakar model .................................................. ........... .................................................. ............ Participating liquid species: myC7H16 Selecting AtomizationModel none Selecting BreakupModel ReitzDiwakar Average parcel mass: 2.4e-10 Selecting radiationModel none No finite volume options present Courant Number mean: 0 max: 0 Starting time loop Courant Number mean: 0 max: 0 deltaT = 2.94118e-06 Time = 2.94118e-06 Solving 3-D cloud sprayCloud Cloud: sprayCloud injector: model1 Added 15 new parcels Cloud: sprayCloud Current number of parcels = 15 Current mass in system = 3.65068e-09 Linear momentum = (3.91847e-09 -7.70137e-07 1.5113e-08) |Linear momentum| = 7.70295e-07 Linear kinetic energy = 8.2358e-05 model1: number of parcels added = 15 mass introduced = 3.65112e-09 Parcel fate (number, mass) - escape = 0, 0 - stick = 0, 0 Temperature min/max = 323.887, 335.398 Mass transfer phase change = 4.33899e-13 D10, D32, Dmax (mu) = 55.0744, 60.0792, 86.0349 Liquid penetration 95% mass (m) = 0.00135545 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 PIMPLE: iteration 1 smoothSolver: Solving for Ux, Initial residual = 1, Final residual = 4.32376e-07, No Iterations 2 smoothSolver: Solving for Uy, Initial residual = 1, Final residual = 4.80901e-07, No Iterations 2 smoothSolver: Solving for Uz, Initial residual = 1, Final residual = 4.73947e-07, No Iterations 2 DILUPBiCG: Solving for myC7H16, Initial residual = 1, Final residual = 1.16637e-07, No Iterations 2 DILUPBiCG: Solving for O2, Initial residual = 0.995339, Final residual = 1.16094e-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 = 0.999985, Final residual = 1.15297e-07, No Iterations 2 T gas min/max = 793.675, 800 .................................................. .................................................. ....................... |
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