|
[Sponsors] |
![]() |
![]() |
#1 |
Senior Member
Join Date: Dec 2019
Posts: 215
Rep Power: 8 ![]() |
Hi,
I am trying to use the kOmegaSSTSAS model with rhoCentralFoam. Unfortunaletely I have some troubles starting a simulation with it. kOmegaSST works fine. When I define my turbulence model like: Code:
simulationType RAS; RAS { RASModel kOmegaSSTSAS; turbulence on; printCoeffs on; kOmegaSSTSASCoeffs { // Default SST coefficients alphaK1 0.85; alphaK2 1.0; alphaOmega1 0.5; alphaOmega2 0.856; beta1 0.075; beta2 0.0828; betaStar 0.09; gamma1 5/9; gamma2 0.44; a1 0.31; b1 1.0; c1 10.0; F3 no; // Default SAS coefficients Cs 0.11; kappa 0.41; zeta2 3.51; sigmaPhi 2.0/3.0; C 2; delta cubeRootVol; cubeRootVolCoeffs { deltaCoeff 1; } } } Code:
--> FOAM FATAL IO ERROR: keyword delta is undefined in dictionary "/home/case_sas/constant/turbulenceProperties.RAS.kOmegaSSTCoeffs" Code:
Mean and max Courant Numbers = 0.01507015757285037026 0.1734610019636567413 deltaT = 1.172882946281961179e-08 Time = 1.172882946281961179e-08 diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0 diagonal: Solving for rhoUx, Initial residual = 0, Final residual = 0, No Iterations 0 diagonal: Solving for rhoUy, Initial residual = 0, Final residual = 0, No Iterations 0 diagonal: Solving for rhoUz, Initial residual = 0, Final residual = 0, No Iterations 0 smoothSolver: Solving for Ux, Initial residual = 0.9983413068152621195, Final residual = 4.523050796451504211e-09, No Iterations 1000 smoothSolver: Solving for Uy, Initial residual = 0.999903823391497748, Final residual = 2.612725370460363529e-10, No Iterations 4 smoothSolver: Solving for Uz, Initial residual = 0.9982737144596987022, Final residual = 4.656112886042951805e-09, No Iterations 1000 diagonal: Solving for rhoE, Initial residual = 0, Final residual = 0, No Iterations 0 smoothSolver: Solving for e, Initial residual = 0.1588687188325532407, Final residual = 2.735319357247494125e-09, No Iterations 1000 #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::sqrt(Foam::Field<double>&, Foam::UList<double> const&) at ??:? #4 Foam::tmp<Foam::GeometricField<double, Foam::fvPatchField, Foam::volMesh> > Foam::sqrt<Foam::fvPatchField, Foam::volMesh>(Foam::tmp<Foam::GeometricField<double, Foam::fvPatchField, Foam::volMesh> > const&) at ??:? #5 Foam::RASModels::kOmegaSSTSAS<Foam::EddyDiffusivity<Foam::ThermalDiffusivity<Foam::CompressibleTurbulenceModel<Foam::fluidThermo> > > >::Qsas(Foam::GeometricField<double, Foam::fvPatchField, Foam::volMesh> const&, Foam::GeometricField<double, Foam::fvPatchField, Foam::volMesh> const&, Foam::GeometricField<double, Foam::fvPatchField, Foam::volMesh> const&) const at ??:? #6 Foam::kOmegaSST<Foam::eddyViscosity<Foam::RASModel<Foam::EddyDiffusivity<Foam::ThermalDiffusivity<Foam::CompressibleTurbulenceModel<Foam::fluidThermo> > > > >, Foam::EddyDiffusivity<Foam::ThermalDiffusivity<Foam::CompressibleTurbulenceModel<Foam::fluidThermo> > > >::correct() at ??:? #7 ? at ??:? #8 __libc_start_main in "/lib/x86_64-linux-gnu/libc.so.6" #9 ? at ??:? Floating point exception (core dumped) |
|
![]() |
![]() |
![]() |
![]() |
#2 |
Senior Member
Join Date: Dec 2019
Posts: 215
Rep Power: 8 ![]() |
This is how it is described in the .H file of the turbulence model.
Code:
References: 34 \verbatim 35 Egorov, Y., & Menter F.R. (2008). 36 Development and Application of SST-SAS Model in the DESIDER Project. 37 Advances in Hybrid RANS-LES Modelling, 38 Notes on Num. Fluid Mech. And Multidisciplinary Design, 39 Volume 97, 261-270. 40 \endverbatim 41 42 The model coefficients are 43 \verbatim 44 kOmegaSSTSASCoeffs 45 { 46 // Default SST coefficients 47 alphaK1 0.85; 48 alphaK2 1.0; 49 alphaOmega1 0.5; 50 alphaOmega2 0.856; 51 beta1 0.075; 52 beta2 0.0828; 53 betaStar 0.09; 54 gamma1 5/9; 55 gamma2 0.44; 56 a1 0.31; 57 b1 1.0; 58 c1 10.0; 59 F3 no; 60 61 // Default SAS coefficients 62 Cs 0.11; 63 kappa 0.41; 64 zeta2 3.51; 65 sigmaPhi 2.0/3.0; 66 C 2; 67 68 // Delta must be specified for SAS e.g. 69 delta cubeRootVol; 70 71 cubeRootVolCoeffs 72 {} 73 } 74 \endverbatim 75 76 SourceFiles 77 kOmegaSSTSAS.C But kOmegaSSTSASCoeffs is not accepted. |
|
![]() |
![]() |
![]() |
![]() |
#3 |
New Member
Marco Rosatti
Join Date: Mar 2019
Location: Argentina
Posts: 4
Rep Power: 8 ![]() |
Hello!, I had a similar problem but trying to run with simpleFoam. I get a
[1] --> FOAM FATAL IO ERROR: [1] keyword delta is undefined in dictionary "IOstream.RAS" |
|
![]() |
![]() |
![]() |
Thread Tools | Search this Thread |
Display Modes | |
|
|
![]() |
||||
Thread | Thread Starter | Forum | Replies | Last Post |
Is COMSOL Multi Physics is suitable to solve complex flow problem? | steve lee | COMSOL | 8 | January 5, 2023 02:31 |
Problem diverges when exhaust valve opens | swerner0711 | AVL FIRE | 0 | September 21, 2018 07:14 |
Gambit - meshing over airfoil wrapping (?) problem | JFDC | FLUENT | 1 | July 11, 2011 05:59 |
natural convection problem for a CHT problem | Se-Hee | CFX | 2 | June 10, 2007 06:29 |
Adiabatic and Rotating wall (Convection problem) | ParodDav | CFX | 5 | April 29, 2007 19:13 |