Given that the number of solid solver modules is currently 1 and unlikely to exceed 3 it is not very useful to maintain solid and fluid sub-directories and easier to see the correspondence between the solver modules and tutorial cases without.
71 lines
2.3 KiB
C++
71 lines
2.3 KiB
C++
/*---------------------------------------------------------------------------*\
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========= |
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\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
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\\ / O peration | Website: https://openfoam.org
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\\ / A nd | Copyright (C) 2022 OpenFOAM Foundation
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\\/ M anipulation |
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-------------------------------------------------------------------------------
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License
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This file is part of OpenFOAM.
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OpenFOAM is free software: you can redistribute it and/or modify it
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under the terms of the GNU General Public License as published by
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the Free Software Foundation, either version 3 of the License, or
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(at your option) any later version.
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OpenFOAM is distributed in the hope that it will be useful, but WITHOUT
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ANY WARRANTY; without even the implied warranty of MERCHANTABILITY or
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FITNESS FOR A PARTICULAR PURPOSE. See the GNU General Public License
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for more details.
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You should have received a copy of the GNU General Public License
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along with OpenFOAM. If not, see <http://www.gnu.org/licenses/>.
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\*---------------------------------------------------------------------------*/
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#include "compressibleVoF.H"
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// * * * * * * * * * * * * * * Member Functions * * * * * * * * * * * * * * //
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void Foam::solvers::compressibleVoF::thermophysicalPredictor()
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{
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volScalarField& T = mixture.T();
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const volScalarField& p = mixture.p();
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const volScalarField& alpha2(mixture.alpha2());
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fvScalarMatrix TEqn
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(
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fvm::ddt(rho, T) + fvm::div(rhoPhi, T) - fvm::Sp(contErr(), T)
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- fvm::laplacian(turbulence.alphaEff(), T)
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+ (
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mixture.totalInternalEnergy()
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?
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fvc::div(fvc::absolute(phi, U), p)()() // - contErr()/rho*p
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+ (fvc::ddt(rho, K) + fvc::div(rhoPhi, K))()()
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- (U()&(fvModels().source(rho, U)&U)()) - contErr()*K
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:
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p*fvc::div(fvc::absolute(phi, U))()()
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)
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*(
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alpha1()/mixture.thermo1().Cv()()
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+ alpha2()/mixture.thermo2().Cv()()
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)
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==
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fvModels().source(rho, T)
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);
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TEqn.relax();
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fvConstraints().constrain(TEqn);
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TEqn.solve();
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fvConstraints().constrain(T);
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mixture.correctThermo();
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mixture.correct();
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}
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// ************************************************************************* //
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