Files
OpenFOAM-6/applications/solvers/multiphase/twoPhaseEulerFoam/twoPhaseSystem/twoPhaseSystem.C
Will Bainbridge f2cc03bf8d MULES: Non-uniform limiting and additional form of limit sum
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.
2018-03-22 16:55:36 +00:00

579 lines
13 KiB
C

/*---------------------------------------------------------------------------*\
========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration |
\\ / A nd | Copyright (C) 2013-2018 OpenFOAM Foundation
\\/ M anipulation |
-------------------------------------------------------------------------------
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 <http://www.gnu.org/licenses/>.
\*---------------------------------------------------------------------------*/
#include "twoPhaseSystem.H"
#include "PhaseCompressibleTurbulenceModel.H"
#include "BlendedInterfacialModel.H"
#include "virtualMassModel.H"
#include "heatTransferModel.H"
#include "liftModel.H"
#include "wallLubricationModel.H"
#include "turbulentDispersionModel.H"
#include "fvMatrix.H"
#include "surfaceInterpolate.H"
#include "MULES.H"
#include "subCycle.H"
#include "fvcDdt.H"
#include "fvcDiv.H"
#include "fvcSnGrad.H"
#include "fvcFlux.H"
#include "fvcCurl.H"
#include "fvmDdt.H"
#include "fvmLaplacian.H"
#include "fixedValueFvsPatchFields.H"
#include "blendingMethod.H"
#include "HashPtrTable.H"
#include "UniformField.H"
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
Foam::twoPhaseSystem::twoPhaseSystem
(
const fvMesh& mesh,
const dimensionedVector& g
)
:
IOdictionary
(
IOobject
(
"phaseProperties",
mesh.time().constant(),
mesh,
IOobject::MUST_READ_IF_MODIFIED,
IOobject::NO_WRITE
)
),
mesh_(mesh),
phase1_
(
*this,
*this,
wordList(lookup("phases"))[0]
),
phase2_
(
*this,
*this,
wordList(lookup("phases"))[1]
),
phi_
(
IOobject
(
"phi",
mesh.time().timeName(),
mesh,
IOobject::NO_READ,
IOobject::AUTO_WRITE
),
this->calcPhi()
),
dgdt_
(
IOobject
(
"dgdt",
mesh.time().timeName(),
mesh,
IOobject::READ_IF_PRESENT,
IOobject::AUTO_WRITE
),
mesh,
dimensionedScalar("dgdt", dimless/dimTime, 0)
)
{
phase2_.volScalarField::operator=(scalar(1) - phase1_);
// Blending
forAllConstIter(dictionary, subDict("blending"), iter)
{
blendingMethods_.insert
(
iter().dict().dictName(),
blendingMethod::New
(
iter().dict(),
wordList(lookup("phases"))
)
);
}
// Pairs
phasePair::scalarTable sigmaTable(lookup("sigma"));
phasePair::dictTable aspectRatioTable(lookup("aspectRatio"));
pair_.set
(
new phasePair
(
phase1_,
phase2_,
g,
sigmaTable
)
);
pair1In2_.set
(
new orderedPhasePair
(
phase1_,
phase2_,
g,
sigmaTable,
aspectRatioTable
)
);
pair2In1_.set
(
new orderedPhasePair
(
phase2_,
phase1_,
g,
sigmaTable,
aspectRatioTable
)
);
// Models
drag_.set
(
new BlendedInterfacialModel<dragModel>
(
lookup("drag"),
(
blendingMethods_.found("drag")
? blendingMethods_["drag"]
: blendingMethods_["default"]
),
pair_,
pair1In2_,
pair2In1_,
false // Do not zero drag coefficient at fixed-flux BCs
)
);
virtualMass_.set
(
new BlendedInterfacialModel<virtualMassModel>
(
lookup("virtualMass"),
(
blendingMethods_.found("virtualMass")
? blendingMethods_["virtualMass"]
: blendingMethods_["default"]
),
pair_,
pair1In2_,
pair2In1_
)
);
heatTransfer_.set
(
new BlendedInterfacialModel<heatTransferModel>
(
lookup("heatTransfer"),
(
blendingMethods_.found("heatTransfer")
? blendingMethods_["heatTransfer"]
: blendingMethods_["default"]
),
pair_,
pair1In2_,
pair2In1_
)
);
lift_.set
(
new BlendedInterfacialModel<liftModel>
(
lookup("lift"),
(
blendingMethods_.found("lift")
? blendingMethods_["lift"]
: blendingMethods_["default"]
),
pair_,
pair1In2_,
pair2In1_
)
);
wallLubrication_.set
(
new BlendedInterfacialModel<wallLubricationModel>
(
lookup("wallLubrication"),
(
blendingMethods_.found("wallLubrication")
? blendingMethods_["wallLubrication"]
: blendingMethods_["default"]
),
pair_,
pair1In2_,
pair2In1_
)
);
turbulentDispersion_.set
(
new BlendedInterfacialModel<turbulentDispersionModel>
(
lookup("turbulentDispersion"),
(
blendingMethods_.found("turbulentDispersion")
? blendingMethods_["turbulentDispersion"]
: blendingMethods_["default"]
),
pair_,
pair1In2_,
pair2In1_
)
);
}
// * * * * * * * * * * * * * * * * Destructor * * * * * * * * * * * * * * * //
Foam::twoPhaseSystem::~twoPhaseSystem()
{}
// * * * * * * * * * * * * * * Member Functions * * * * * * * * * * * * * * //
Foam::tmp<Foam::volScalarField> Foam::twoPhaseSystem::rho() const
{
return phase1_*phase1_.thermo().rho() + phase2_*phase2_.thermo().rho();
}
Foam::tmp<Foam::volVectorField> Foam::twoPhaseSystem::U() const
{
return phase1_*phase1_.U() + phase2_*phase2_.U();
}
Foam::tmp<Foam::surfaceScalarField> Foam::twoPhaseSystem::calcPhi() const
{
return
fvc::interpolate(phase1_)*phase1_.phi()
+ fvc::interpolate(phase2_)*phase2_.phi();
}
Foam::tmp<Foam::volScalarField> Foam::twoPhaseSystem::Kd() const
{
return drag_->K();
}
Foam::tmp<Foam::surfaceScalarField> Foam::twoPhaseSystem::Kdf() const
{
return drag_->Kf();
}
Foam::tmp<Foam::volScalarField> Foam::twoPhaseSystem::Vm() const
{
return virtualMass_->K();
}
Foam::tmp<Foam::surfaceScalarField> Foam::twoPhaseSystem::Vmf() const
{
return virtualMass_->Kf();
}
Foam::tmp<Foam::volScalarField> Foam::twoPhaseSystem::Kh() const
{
return heatTransfer_->K();
}
Foam::tmp<Foam::volVectorField> Foam::twoPhaseSystem::F() const
{
return lift_->F<vector>() + wallLubrication_->F<vector>();
}
Foam::tmp<Foam::surfaceScalarField> Foam::twoPhaseSystem::Ff() const
{
return lift_->Ff() + wallLubrication_->Ff();
}
Foam::tmp<Foam::volScalarField> Foam::twoPhaseSystem::D() const
{
return turbulentDispersion_->D();
}
void Foam::twoPhaseSystem::solve()
{
const Time& runTime = mesh_.time();
volScalarField& alpha1 = phase1_;
volScalarField& alpha2 = phase2_;
const surfaceScalarField& phi1 = phase1_.phi();
const surfaceScalarField& phi2 = phase2_.phi();
const dictionary& alphaControls = mesh_.solverDict
(
alpha1.name()
);
label nAlphaSubCycles(readLabel(alphaControls.lookup("nAlphaSubCycles")));
label nAlphaCorr(readLabel(alphaControls.lookup("nAlphaCorr")));
word alphaScheme("div(phi," + alpha1.name() + ')');
word alpharScheme("div(phir," + alpha1.name() + ')');
alpha1.correctBoundaryConditions();
surfaceScalarField phic("phic", phi_);
surfaceScalarField phir("phir", phi1 - phi2);
tmp<surfaceScalarField> alpha1alpha2f;
if (pPrimeByA_.valid())
{
alpha1alpha2f =
fvc::interpolate(max(alpha1, scalar(0)))
*fvc::interpolate(max(alpha2, scalar(0)));
surfaceScalarField phiP
(
pPrimeByA_()*fvc::snGrad(alpha1, "bounded")*mesh_.magSf()
);
phir += phiP;
}
for (int acorr=0; acorr<nAlphaCorr; acorr++)
{
volScalarField::Internal Sp
(
IOobject
(
"Sp",
runTime.timeName(),
mesh_
),
mesh_,
dimensionedScalar("Sp", dgdt_.dimensions(), 0.0)
);
volScalarField::Internal Su
(
IOobject
(
"Su",
runTime.timeName(),
mesh_
),
// Divergence term is handled explicitly to be
// consistent with the explicit transport solution
fvc::div(phi_)*min(alpha1, scalar(1))
);
forAll(dgdt_, celli)
{
if (dgdt_[celli] > 0.0)
{
Sp[celli] -= dgdt_[celli]/max(1.0 - alpha1[celli], 1e-4);
Su[celli] += dgdt_[celli]/max(1.0 - alpha1[celli], 1e-4);
}
else if (dgdt_[celli] < 0.0)
{
Sp[celli] += dgdt_[celli]/max(alpha1[celli], 1e-4);
}
}
surfaceScalarField alphaPhic1
(
fvc::flux
(
phic,
alpha1,
alphaScheme
)
+ fvc::flux
(
-fvc::flux(-phir, scalar(1) - alpha1, alpharScheme),
alpha1,
alpharScheme
)
);
phase1_.correctInflowOutflow(alphaPhic1);
if (nAlphaSubCycles > 1)
{
for
(
subCycle<volScalarField> alphaSubCycle(alpha1, nAlphaSubCycles);
!(++alphaSubCycle).end();
)
{
surfaceScalarField alphaPhic10(alphaPhic1);
MULES::explicitSolve
(
geometricOneField(),
alpha1,
phi_,
alphaPhic10,
(alphaSubCycle.index()*Sp)(),
(Su - (alphaSubCycle.index() - 1)*Sp*alpha1)(),
UniformField<scalar>(phase1_.alphaMax()),
zeroField()
);
if (alphaSubCycle.index() == 1)
{
phase1_.alphaPhi() = alphaPhic10;
}
else
{
phase1_.alphaPhi() += alphaPhic10;
}
}
phase1_.alphaPhi() /= nAlphaSubCycles;
}
else
{
MULES::explicitSolve
(
geometricOneField(),
alpha1,
phi_,
alphaPhic1,
Sp,
Su,
UniformField<scalar>(phase1_.alphaMax()),
zeroField()
);
phase1_.alphaPhi() = alphaPhic1;
}
if (pPrimeByA_.valid())
{
fvScalarMatrix alpha1Eqn
(
fvm::ddt(alpha1) - fvc::ddt(alpha1)
- fvm::laplacian(alpha1alpha2f()*pPrimeByA_(), alpha1, "bounded")
);
alpha1Eqn.relax();
alpha1Eqn.solve();
phase1_.alphaPhi() += alpha1Eqn.flux();
}
phase1_.alphaRhoPhi() =
fvc::interpolate(phase1_.rho())*phase1_.alphaPhi();
phase2_.alphaPhi() = phi_ - phase1_.alphaPhi();
phase2_.correctInflowOutflow(phase2_.alphaPhi());
phase2_.alphaRhoPhi() =
fvc::interpolate(phase2_.rho())*phase2_.alphaPhi();
Info<< alpha1.name() << " volume fraction = "
<< alpha1.weightedAverage(mesh_.V()).value()
<< " Min(" << alpha1.name() << ") = " << min(alpha1).value()
<< " Max(" << alpha1.name() << ") = " << max(alpha1).value()
<< endl;
// Ensure the phase-fractions are bounded
alpha1.max(0);
alpha1.min(1);
alpha2 = scalar(1) - alpha1;
}
}
void Foam::twoPhaseSystem::correct()
{
phase1_.correct();
phase2_.correct();
}
void Foam::twoPhaseSystem::correctTurbulence()
{
phase1_.turbulence().correct();
phase2_.turbulence().correct();
}
bool Foam::twoPhaseSystem::read()
{
if (regIOobject::read())
{
bool readOK = true;
readOK &= phase1_.read(*this);
readOK &= phase2_.read(*this);
// models ...
return readOK;
}
else
{
return false;
}
}
const Foam::dimensionedScalar& Foam::twoPhaseSystem::sigma() const
{
return pair_->sigma();
}
// ************************************************************************* //