/*---------------------------------------------------------------------------*\ ========= | \\ / F ield | OpenFOAM: The Open Source CFD Toolbox \\ / O peration | \\ / A nd | www.openfoam.com \\/ M anipulation | ------------------------------------------------------------------------------- Copyright (C) 2011-2017 OpenFOAM Foundation Copyright (C) 2019 OpenCFD Ltd. ------------------------------------------------------------------------------- License This file is part of OpenFOAM. OpenFOAM is free software: you can redistribute it and/or modify it under the terms of the GNU General Public License as published by the Free Software Foundation, either version 3 of the License, or (at your option) any later version. OpenFOAM is distributed in the hope that it will be useful, but WITHOUT ANY WARRANTY; without even the implied warranty of MERCHANTABILITY or FITNESS FOR A PARTICULAR PURPOSE. See the GNU General Public License for more details. You should have received a copy of the GNU General Public License along with OpenFOAM. If not, see . Application compressibleInterDyMFoam Description Solver for two compressible, non-isothermal immiscible fluids using a VOF (volume of fluid) phase-fraction based interface capturing approach, with optional mesh motion and mesh topology changes including adaptive re-meshing. The momentum and other fluid properties are of the "mixture" and a single momentum equation is solved. Turbulence modelling is generic, i.e. laminar, RAS or LES may be selected. \*---------------------------------------------------------------------------*/ #include "fvCFD.H" #include "dynamicFvMesh.H" #include "CMULES.H" #include "EulerDdtScheme.H" #include "localEulerDdtScheme.H" #include "CrankNicolsonDdtScheme.H" #include "subCycle.H" #include "compressibleInterPhaseTransportModel.H" #include "pimpleControl.H" #include "fvOptions.H" #include "CorrectPhi.H" #include "fvcSmooth.H" // * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * // int main(int argc, char *argv[]) { argList::addNote ( "Solver for two compressible, non-isothermal immiscible fluids" " using VOF phase-fraction based interface capturing.\n" "With optional mesh motion and mesh topology changes including" " adaptive re-meshing." ); #include "postProcess.H" #include "setRootCaseLists.H" #include "createTime.H" #include "createDynamicFvMesh.H" #include "initContinuityErrs.H" #include "createDyMControls.H" #include "createFields.H" #include "createUf.H" #include "CourantNo.H" #include "setInitialDeltaT.H" volScalarField& p = mixture.p(); volScalarField& T = mixture.T(); const volScalarField& psi1 = mixture.thermo1().psi(); const volScalarField& psi2 = mixture.thermo2().psi(); // * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * // Info<< "\nStarting time loop\n" << endl; while (runTime.run()) { #include "readDyMControls.H" // Store divU and divUp from the previous mesh so that it can be mapped // and used in correctPhi to ensure the corrected phi has the // same divergence volScalarField divU("divU0", fvc::div(fvc::absolute(phi, U))); volScalarField divUp("divUp", fvc::div(fvc::absolute(phi, U), p)); if (LTS) { #include "setRDeltaT.H" } else { #include "CourantNo.H" #include "alphaCourantNo.H" #include "setDeltaT.H" } ++runTime; Info<< "Time = " << runTime.timeName() << nl << endl; // --- Pressure-velocity PIMPLE corrector loop while (pimple.loop()) { if (pimple.firstIter() || moveMeshOuterCorrectors) { scalar timeBeforeMeshUpdate = runTime.elapsedCpuTime(); mesh.update(); if (mesh.changing()) { MRF.update(); Info<< "Execution time for mesh.update() = " << runTime.elapsedCpuTime() - timeBeforeMeshUpdate << " s" << endl; gh = (g & mesh.C()) - ghRef; ghf = (g & mesh.Cf()) - ghRef; } if ((mesh.changing() && correctPhi)) { // Calculate absolute flux from the mapped surface velocity phi = mesh.Sf() & Uf; #include "correctPhi.H" // Make the fluxes relative to the mesh motion fvc::makeRelative(phi, U); mixture.correct(); } if (mesh.changing() && checkMeshCourantNo) { #include "meshCourantNo.H" } } #include "alphaControls.H" #include "compressibleAlphaEqnSubCycle.H" turbulence.correctPhasePhi(); #include "UEqn.H" #include "TEqn.H" // --- Pressure corrector loop while (pimple.correct()) { #include "pEqn.H" } if (pimple.turbCorr()) { turbulence.correct(); } } rho = alpha1*rho1 + alpha2*rho2; // Correct p_rgh for consistency with p and the updated densities p_rgh = p - rho*gh; p_rgh.correctBoundaryConditions(); runTime.write(); runTime.printExecutionTime(Info); } Info<< "End\n" << endl; return 0; } // ************************************************************************* //