mirror of
https://github.com/OpenFOAM/OpenFOAM-6.git
synced 2025-12-08 06:57:46 +00:00
MULES and CMULES have been extended so that the limits can be supplied as fields. These arguments are templated so that zeroField, oneField or UniformField<scalar> can be used in place of a scalar value with no additional overhead. The flux argument has been removed from the unlimited CMULES correct functions in order to make this templating possible. An additional form of limit sum has also been added to MULES. This limits the flux sum by ofsetting in proportion to the phase fraction, rather than by reducing the magnitude of the fluxes with the same sign as the imbalance. The new procedure makes it possible to limit the flux sum in the presence of constraints without encountering a divide by zero.
579 lines
13 KiB
C
579 lines
13 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 | Copyright (C) 2013-2018 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 "twoPhaseSystem.H"
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#include "PhaseCompressibleTurbulenceModel.H"
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#include "BlendedInterfacialModel.H"
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#include "virtualMassModel.H"
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#include "heatTransferModel.H"
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#include "liftModel.H"
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#include "wallLubricationModel.H"
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#include "turbulentDispersionModel.H"
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#include "fvMatrix.H"
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#include "surfaceInterpolate.H"
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#include "MULES.H"
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#include "subCycle.H"
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#include "fvcDdt.H"
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#include "fvcDiv.H"
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#include "fvcSnGrad.H"
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#include "fvcFlux.H"
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#include "fvcCurl.H"
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#include "fvmDdt.H"
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#include "fvmLaplacian.H"
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#include "fixedValueFvsPatchFields.H"
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#include "blendingMethod.H"
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#include "HashPtrTable.H"
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#include "UniformField.H"
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// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
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Foam::twoPhaseSystem::twoPhaseSystem
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(
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const fvMesh& mesh,
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const dimensionedVector& g
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)
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:
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IOdictionary
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(
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IOobject
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(
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"phaseProperties",
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mesh.time().constant(),
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mesh,
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IOobject::MUST_READ_IF_MODIFIED,
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IOobject::NO_WRITE
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)
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),
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mesh_(mesh),
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phase1_
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(
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*this,
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*this,
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wordList(lookup("phases"))[0]
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),
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phase2_
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(
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*this,
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*this,
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wordList(lookup("phases"))[1]
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),
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phi_
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(
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IOobject
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(
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"phi",
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mesh.time().timeName(),
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mesh,
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IOobject::NO_READ,
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IOobject::AUTO_WRITE
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),
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this->calcPhi()
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),
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dgdt_
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(
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IOobject
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(
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"dgdt",
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mesh.time().timeName(),
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mesh,
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IOobject::READ_IF_PRESENT,
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IOobject::AUTO_WRITE
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),
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mesh,
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dimensionedScalar("dgdt", dimless/dimTime, 0)
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)
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{
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phase2_.volScalarField::operator=(scalar(1) - phase1_);
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// Blending
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forAllConstIter(dictionary, subDict("blending"), iter)
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{
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blendingMethods_.insert
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(
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iter().dict().dictName(),
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blendingMethod::New
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(
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iter().dict(),
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wordList(lookup("phases"))
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)
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);
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}
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// Pairs
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phasePair::scalarTable sigmaTable(lookup("sigma"));
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phasePair::dictTable aspectRatioTable(lookup("aspectRatio"));
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pair_.set
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(
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new phasePair
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(
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phase1_,
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phase2_,
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g,
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sigmaTable
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)
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);
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pair1In2_.set
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(
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new orderedPhasePair
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(
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phase1_,
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phase2_,
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g,
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sigmaTable,
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aspectRatioTable
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)
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);
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pair2In1_.set
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(
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new orderedPhasePair
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(
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phase2_,
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phase1_,
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g,
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sigmaTable,
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aspectRatioTable
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)
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);
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// Models
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drag_.set
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(
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new BlendedInterfacialModel<dragModel>
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(
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lookup("drag"),
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(
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blendingMethods_.found("drag")
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? blendingMethods_["drag"]
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: blendingMethods_["default"]
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),
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pair_,
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pair1In2_,
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pair2In1_,
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false // Do not zero drag coefficient at fixed-flux BCs
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)
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);
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virtualMass_.set
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(
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new BlendedInterfacialModel<virtualMassModel>
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(
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lookup("virtualMass"),
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(
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blendingMethods_.found("virtualMass")
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? blendingMethods_["virtualMass"]
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: blendingMethods_["default"]
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),
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pair_,
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pair1In2_,
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pair2In1_
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)
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);
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heatTransfer_.set
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(
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new BlendedInterfacialModel<heatTransferModel>
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(
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lookup("heatTransfer"),
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(
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blendingMethods_.found("heatTransfer")
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? blendingMethods_["heatTransfer"]
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: blendingMethods_["default"]
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),
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pair_,
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pair1In2_,
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pair2In1_
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)
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);
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lift_.set
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(
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new BlendedInterfacialModel<liftModel>
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(
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lookup("lift"),
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(
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blendingMethods_.found("lift")
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? blendingMethods_["lift"]
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: blendingMethods_["default"]
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),
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pair_,
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pair1In2_,
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pair2In1_
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)
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);
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wallLubrication_.set
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(
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new BlendedInterfacialModel<wallLubricationModel>
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(
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lookup("wallLubrication"),
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(
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blendingMethods_.found("wallLubrication")
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? blendingMethods_["wallLubrication"]
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: blendingMethods_["default"]
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),
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pair_,
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pair1In2_,
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pair2In1_
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)
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);
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turbulentDispersion_.set
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(
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new BlendedInterfacialModel<turbulentDispersionModel>
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(
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lookup("turbulentDispersion"),
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(
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blendingMethods_.found("turbulentDispersion")
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? blendingMethods_["turbulentDispersion"]
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: blendingMethods_["default"]
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),
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pair_,
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pair1In2_,
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pair2In1_
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)
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);
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}
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// * * * * * * * * * * * * * * * * Destructor * * * * * * * * * * * * * * * //
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Foam::twoPhaseSystem::~twoPhaseSystem()
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{}
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// * * * * * * * * * * * * * * Member Functions * * * * * * * * * * * * * * //
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Foam::tmp<Foam::volScalarField> Foam::twoPhaseSystem::rho() const
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{
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return phase1_*phase1_.thermo().rho() + phase2_*phase2_.thermo().rho();
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}
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Foam::tmp<Foam::volVectorField> Foam::twoPhaseSystem::U() const
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{
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return phase1_*phase1_.U() + phase2_*phase2_.U();
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}
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Foam::tmp<Foam::surfaceScalarField> Foam::twoPhaseSystem::calcPhi() const
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{
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return
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fvc::interpolate(phase1_)*phase1_.phi()
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+ fvc::interpolate(phase2_)*phase2_.phi();
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}
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Foam::tmp<Foam::volScalarField> Foam::twoPhaseSystem::Kd() const
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{
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return drag_->K();
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}
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Foam::tmp<Foam::surfaceScalarField> Foam::twoPhaseSystem::Kdf() const
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{
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return drag_->Kf();
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}
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Foam::tmp<Foam::volScalarField> Foam::twoPhaseSystem::Vm() const
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{
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return virtualMass_->K();
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}
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Foam::tmp<Foam::surfaceScalarField> Foam::twoPhaseSystem::Vmf() const
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{
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return virtualMass_->Kf();
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}
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Foam::tmp<Foam::volScalarField> Foam::twoPhaseSystem::Kh() const
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{
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return heatTransfer_->K();
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}
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Foam::tmp<Foam::volVectorField> Foam::twoPhaseSystem::F() const
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{
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return lift_->F<vector>() + wallLubrication_->F<vector>();
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}
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Foam::tmp<Foam::surfaceScalarField> Foam::twoPhaseSystem::Ff() const
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{
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return lift_->Ff() + wallLubrication_->Ff();
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}
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Foam::tmp<Foam::volScalarField> Foam::twoPhaseSystem::D() const
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{
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return turbulentDispersion_->D();
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}
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void Foam::twoPhaseSystem::solve()
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{
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const Time& runTime = mesh_.time();
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volScalarField& alpha1 = phase1_;
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volScalarField& alpha2 = phase2_;
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const surfaceScalarField& phi1 = phase1_.phi();
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const surfaceScalarField& phi2 = phase2_.phi();
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const dictionary& alphaControls = mesh_.solverDict
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(
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alpha1.name()
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);
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label nAlphaSubCycles(readLabel(alphaControls.lookup("nAlphaSubCycles")));
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label nAlphaCorr(readLabel(alphaControls.lookup("nAlphaCorr")));
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word alphaScheme("div(phi," + alpha1.name() + ')');
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word alpharScheme("div(phir," + alpha1.name() + ')');
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alpha1.correctBoundaryConditions();
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surfaceScalarField phic("phic", phi_);
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surfaceScalarField phir("phir", phi1 - phi2);
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tmp<surfaceScalarField> alpha1alpha2f;
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if (pPrimeByA_.valid())
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{
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alpha1alpha2f =
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fvc::interpolate(max(alpha1, scalar(0)))
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*fvc::interpolate(max(alpha2, scalar(0)));
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surfaceScalarField phiP
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(
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pPrimeByA_()*fvc::snGrad(alpha1, "bounded")*mesh_.magSf()
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);
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phir += phiP;
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}
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for (int acorr=0; acorr<nAlphaCorr; acorr++)
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{
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volScalarField::Internal Sp
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(
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IOobject
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(
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"Sp",
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runTime.timeName(),
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mesh_
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),
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mesh_,
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dimensionedScalar("Sp", dgdt_.dimensions(), 0.0)
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);
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volScalarField::Internal Su
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(
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IOobject
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(
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"Su",
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runTime.timeName(),
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mesh_
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),
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// Divergence term is handled explicitly to be
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// consistent with the explicit transport solution
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fvc::div(phi_)*min(alpha1, scalar(1))
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);
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forAll(dgdt_, celli)
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{
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if (dgdt_[celli] > 0.0)
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{
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Sp[celli] -= dgdt_[celli]/max(1.0 - alpha1[celli], 1e-4);
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Su[celli] += dgdt_[celli]/max(1.0 - alpha1[celli], 1e-4);
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}
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else if (dgdt_[celli] < 0.0)
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{
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Sp[celli] += dgdt_[celli]/max(alpha1[celli], 1e-4);
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}
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}
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surfaceScalarField alphaPhic1
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(
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fvc::flux
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(
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phic,
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alpha1,
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alphaScheme
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)
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+ fvc::flux
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(
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-fvc::flux(-phir, scalar(1) - alpha1, alpharScheme),
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alpha1,
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alpharScheme
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)
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);
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phase1_.correctInflowOutflow(alphaPhic1);
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if (nAlphaSubCycles > 1)
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{
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for
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(
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subCycle<volScalarField> alphaSubCycle(alpha1, nAlphaSubCycles);
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!(++alphaSubCycle).end();
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)
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{
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surfaceScalarField alphaPhic10(alphaPhic1);
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MULES::explicitSolve
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(
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geometricOneField(),
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alpha1,
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phi_,
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alphaPhic10,
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(alphaSubCycle.index()*Sp)(),
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(Su - (alphaSubCycle.index() - 1)*Sp*alpha1)(),
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UniformField<scalar>(phase1_.alphaMax()),
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zeroField()
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);
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if (alphaSubCycle.index() == 1)
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{
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phase1_.alphaPhi() = alphaPhic10;
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}
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else
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{
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phase1_.alphaPhi() += alphaPhic10;
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}
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}
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phase1_.alphaPhi() /= nAlphaSubCycles;
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}
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else
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{
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MULES::explicitSolve
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(
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geometricOneField(),
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alpha1,
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phi_,
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alphaPhic1,
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Sp,
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Su,
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UniformField<scalar>(phase1_.alphaMax()),
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zeroField()
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);
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phase1_.alphaPhi() = alphaPhic1;
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}
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if (pPrimeByA_.valid())
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{
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fvScalarMatrix alpha1Eqn
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(
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fvm::ddt(alpha1) - fvc::ddt(alpha1)
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- fvm::laplacian(alpha1alpha2f()*pPrimeByA_(), alpha1, "bounded")
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);
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alpha1Eqn.relax();
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alpha1Eqn.solve();
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phase1_.alphaPhi() += alpha1Eqn.flux();
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}
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phase1_.alphaRhoPhi() =
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fvc::interpolate(phase1_.rho())*phase1_.alphaPhi();
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phase2_.alphaPhi() = phi_ - phase1_.alphaPhi();
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phase2_.correctInflowOutflow(phase2_.alphaPhi());
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phase2_.alphaRhoPhi() =
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fvc::interpolate(phase2_.rho())*phase2_.alphaPhi();
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Info<< alpha1.name() << " volume fraction = "
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<< alpha1.weightedAverage(mesh_.V()).value()
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<< " Min(" << alpha1.name() << ") = " << min(alpha1).value()
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<< " Max(" << alpha1.name() << ") = " << max(alpha1).value()
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<< endl;
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// Ensure the phase-fractions are bounded
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alpha1.max(0);
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alpha1.min(1);
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alpha2 = scalar(1) - alpha1;
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}
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}
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|
|
|
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void Foam::twoPhaseSystem::correct()
|
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{
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phase1_.correct();
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phase2_.correct();
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}
|
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|
|
|
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void Foam::twoPhaseSystem::correctTurbulence()
|
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{
|
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phase1_.turbulence().correct();
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phase2_.turbulence().correct();
|
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}
|
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|
|
|
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bool Foam::twoPhaseSystem::read()
|
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{
|
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if (regIOobject::read())
|
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{
|
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bool readOK = true;
|
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readOK &= phase1_.read(*this);
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readOK &= phase2_.read(*this);
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// models ...
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return readOK;
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}
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else
|
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{
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return false;
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}
|
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}
|
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|
|
|
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const Foam::dimensionedScalar& Foam::twoPhaseSystem::sigma() const
|
|
{
|
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return pair_->sigma();
|
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}
|
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|
|
|
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// ************************************************************************* //
|