3e43edf056
- previously introduced `getOrDefault` as a dictionary _get_ method, now complete the transition and use it everywhere instead of `lookupOrDefault`. This avoids mixed usage of the two methods that are identical in behaviour, makes for shorter names, and promotes the distinction between "lookup" access (ie, return a token stream, locate and return an entry) and "get" access (ie, the above with conversion to concrete types such as scalar, label etc).
134 lines
3.6 KiB
C
134 lines
3.6 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) 2011-2016 OpenFOAM Foundation
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Copyright (C) 2020 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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multiphaseEulerFoam
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Group
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grpMultiphaseSolvers
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Description
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Solver for a system of many compressible fluid phases including
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heat-transfer.
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\*---------------------------------------------------------------------------*/
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#include "fvCFD.H"
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#include "multiphaseSystem.H"
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#include "phaseModel.H"
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#include "dragModel.H"
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#include "heatTransferModel.H"
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#include "singlePhaseTransportModel.H"
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#include "turbulentTransportModel.H"
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#include "pimpleControl.H"
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#include "IOMRFZoneList.H"
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#include "CorrectPhi.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 a system of many compressible fluid phases including"
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" heat-transfer."
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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 "createFields.H"
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#include "initContinuityErrs.H"
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#include "createTimeControls.H"
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#include "correctPhi.H"
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#include "CourantNo.H"
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#include "setInitialDeltaT.H"
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scalar slamDampCoeff
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(
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fluid.getOrDefault<scalar>("slamDampCoeff", 1)
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);
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dimensionedScalar maxSlamVelocity
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(
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"maxSlamVelocity",
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dimVelocity,
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GREAT,
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fluid
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);
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turbulence->validate();
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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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#include "CourantNo.H"
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#include "setDeltaT.H"
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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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turbulence->correct();
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fluid.solve();
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rho = fluid.rho();
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#include "zonePhaseVolumes.H"
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//#include "TEqns.H"
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#include "UEqns.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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#include "DDtU.H"
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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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