149 lines
4.3 KiB
C
149 lines
4.3 KiB
C
/*---------------------------------------------------------------------------*\
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========= |
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\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
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\\ / O peration |
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\\ / A nd | www.openfoam.com
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\\/ M anipulation |
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-------------------------------------------------------------------------------
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Copyright (C) 2011-2017 OpenFOAM Foundation
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Copyright (C) OpenCFD OpenCFD Ltd.
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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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Application
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compressibleInterFoam
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Group
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grpMultiphaseSolvers
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Description
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Solver for two compressible, non-isothermal immiscible fluids using a VOF
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(volume of fluid) phase-fraction based interface capturing approach.
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The momentum and other fluid properties are of the "mixture" and a single
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momentum equation is solved.
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Either mixture or two-phase transport modelling may be selected. In the
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mixture approach a single laminar, RAS or LES model is selected to model the
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momentum stress. In the Euler-Euler two-phase approach separate laminar,
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RAS or LES selected models are selected for each of the phases.
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\*---------------------------------------------------------------------------*/
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#include "fvCFD.H"
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#include "CMULES.H"
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#include "EulerDdtScheme.H"
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#include "localEulerDdtScheme.H"
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#include "CrankNicolsonDdtScheme.H"
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#include "subCycle.H"
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#include "compressibleInterPhaseTransportModel.H"
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#include "pimpleControl.H"
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#include "fvOptions.H"
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#include "fvcSmooth.H"
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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int main(int argc, char *argv[])
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{
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argList::addNote
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(
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"Solver for two compressible, non-isothermal immiscible fluids"
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" using VOF phase-fraction based interface capturing."
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);
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#include "postProcess.H"
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#include "addCheckCaseOptions.H"
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#include "setRootCaseLists.H"
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#include "createTime.H"
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#include "createMesh.H"
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#include "createControl.H"
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#include "createTimeControls.H"
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#include "createFields.H"
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volScalarField& p = mixture.p();
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volScalarField& T = mixture.T();
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const volScalarField& psi1 = mixture.thermo1().psi();
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const volScalarField& psi2 = mixture.thermo2().psi();
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if (!LTS)
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{
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#include "readTimeControls.H"
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#include "CourantNo.H"
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#include "setInitialDeltaT.H"
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}
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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Info<< "\nStarting time loop\n" << endl;
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while (runTime.run())
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{
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#include "readTimeControls.H"
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if (LTS)
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{
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#include "setRDeltaT.H"
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}
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else
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{
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#include "CourantNo.H"
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#include "alphaCourantNo.H"
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#include "setDeltaT.H"
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}
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++runTime;
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Info<< "Time = " << runTime.timeName() << nl << endl;
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// --- Pressure-velocity PIMPLE corrector loop
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while (pimple.loop())
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{
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#include "alphaControls.H"
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#include "compressibleAlphaEqnSubCycle.H"
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turbulence.correctPhasePhi();
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#include "UEqn.H"
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volScalarField divUp("divUp", fvc::div(fvc::absolute(phi, U), p));
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#include "TEqn.H"
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// --- Pressure corrector loop
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while (pimple.correct())
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{
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#include "pEqn.H"
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}
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if (pimple.turbCorr())
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{
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turbulence.correct();
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}
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}
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runTime.write();
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runTime.printExecutionTime(Info);
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}
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Info<< "End\n" << endl;
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return 0;
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}
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// ************************************************************************* //
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