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Commit ea17556c authored by shunbo's avatar shunbo
Browse files

Initial commit

parents
rho = thermo.rho();
volScalarField rAU(1.0/UEqn.A());
volScalarField rAtU(1.0/(1.0/rAU - UEqn.H1()));
volVectorField HbyA(constrainHbyA(rAU*UEqn.H(), U, p));
if (pimple.nCorrPISO() <= 1)
{
tUEqn.clear();
}
if (pimple.transonic())
{
surfaceScalarField phid
(
"phid",
fvc::interpolate(psi)
*(
fvc::flux(HbyA)
+ MRF.zeroFilter
(
fvc::interpolate(rho*rAU)*fvc::ddtCorr(rho, U, phi)
/fvc::interpolate(rho)
)
)
);
MRF.makeRelative(fvc::interpolate(psi), phid);
surfaceScalarField phic
(
"phic",
fvc::interpolate(rho*(rAtU - rAU))*fvc::snGrad(p)*mesh.magSf()
);
HbyA -= (rAU - rAtU)*fvc::grad(p);
volScalarField rhorAtU("rhorAtU", rho*rAtU);
while (pimple.correctNonOrthogonal())
{
fvScalarMatrix pEqn
(
fvm::ddt(psi, p)
+ fvm::div(phid, p)
+ fvc::div(phic)
- fvm::laplacian(rhorAtU, p)
==
fvOptions(psi, p, rho.name())
);
pEqn.solve(mesh.solver(p.select(pimple.finalInnerIter())));
if (pimple.finalNonOrthogonalIter())
{
phi == phic + pEqn.flux();
}
}
}
else
{
surfaceScalarField phiHbyA
(
"phiHbyA",
(
fvc::flux(rho*HbyA)
+ MRF.zeroFilter(fvc::interpolate(rho*rAU)*fvc::ddtCorr(rho, U, phi))
)
);
MRF.makeRelative(fvc::interpolate(rho), phiHbyA);
phiHbyA += fvc::interpolate(rho*(rAtU - rAU))*fvc::snGrad(p)*mesh.magSf();
HbyA -= (rAU - rAtU)*fvc::grad(p);
volScalarField rhorAtU("rhorAtU", rho*rAtU);
// Update the pressure BCs to ensure flux consistency
constrainPressure(p, rho, U, phiHbyA, rhorAtU, MRF);
while (pimple.correctNonOrthogonal())
{
fvScalarMatrix pEqn
(
fvm::ddt(psi, p)
+ fvc::div(phiHbyA)
- fvm::laplacian(rhorAtU, p)
==
fvOptions(psi, p, rho.name())
);
pEqn.solve(mesh.solver(p.select(pimple.finalInnerIter())));
if (pimple.finalNonOrthogonalIter())
{
phi = phiHbyA + pEqn.flux();
}
}
}
#include "rhoEqn.H"
#include "compressibleContinuityErrs.H"
// Explicitly relax pressure for momentum corrector
p.relax();
U = HbyA - rAtU*fvc::grad(p);
U.correctBoundaryConditions();
fvOptions.correct(U);
K = 0.5*magSqr(U);
if (pressureControl.limit(p))
{
p.correctBoundaryConditions();
rho = thermo.rho();
}
if (thermo.dpdt())
{
dpdt = fvc::ddt(p);
}
/*---------------------------------------------------------------------------*\
========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration |
\\ / A nd | www.openfoam.com
\\/ M anipulation |
-------------------------------------------------------------------------------
Copyright (C) 2011-2017 OpenFOAM Foundation
-------------------------------------------------------------------------------
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/>.
Application
reactingFoam
Group
grpCombustionSolvers
Description
Solver for combustion with chemical reactions.
\*---------------------------------------------------------------------------*/
#include "fvCFD.H"
#include "gpufvCFD.H"
#include "turbulentFluidThermoModel.H"
#include "psiReactionThermo.H"
#include "CombustionModel.H"
#include "multivariateScheme.H"
#include "pimpleControl.H"
#include "pressureControl.H"
#include "fvOptions.H"
#include "localEulerDdtScheme.H"
#include "fvcSmooth.H"
#include <sys/time.h>
struct my_timer
{
struct timeval start_time, end_time;
double time_use;
void start()
{
gettimeofday(&start_time, NULL);
}
void stop()
{
gettimeofday(&end_time, NULL);
time_use = (end_time.tv_sec - start_time.tv_sec) + (double)(end_time.tv_usec - start_time.tv_usec)/1000000.0;
}
};
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
int main(int argc, char *argv[])
{
argList::addNote
(
"Solver for combustion with chemical reactions"
);
#include "postProcess.H"
#include "addCheckCaseOptions.H"
#include "setRootCaseLists.H"
#include "createTime.H"
#include "gpucreateMesh.H"
#include "createControl.H"
#include "createTimeControls.H"
#include "initContinuityErrs.H"
#include "createFields.H"
#include "createFieldRefs.H"
double totalYEqntime=0.0;
turbulence->validate();
if (!LTS)
{
#include "compressibleCourantNo.H"
#include "setInitialDeltaT.H"
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
Info<< "\nStarting time loop\n" << endl;
while (runTime.run())
{
#include "readTimeControls.H"
if (LTS)
{
#include "setRDeltaT.H"
}
else
{
#include "compressibleCourantNo.H"
#include "setDeltaT.H"
}
++runTime;
Info<< "Time = " << runTime.timeName() << nl << endl;
#include "rhoEqn.H"
while (pimple.loop())
{
#include "UEqn.H"
my_timer tm;
tm.start();
#include "YEqn.H"
tm.stop();
Info<<"------Timecost YEqn = "<<tm.time_use<<"s-------------------"<< nl << endl;
totalYEqntime+=tm.time_use;
#include "EEqn.H"
// --- Pressure corrector loop
while (pimple.correct())
{
if (pimple.consistent())
{
#include "pcEqn.H"
}
else
{
#include "pEqn.H"
}
}
if (pimple.turbCorr())
{
turbulence->correct();
}
}
rho = thermo.rho();
runTime.write();
runTime.printExecutionTime(Info);
}
Info<<"------TotalTimecost YEqn = "<<totalYEqntime<<"s-------------------"<< nl << endl;
Info<< "End\n" << endl;
return 0;
}
// ************************************************************************* //
rhoReactingBuoyantFoam.C
EXE = $(FOAM_APPBIN)/rhoReactingBuoyantFoam
EXE_INC = \
-I$(FOAM_SOLVERS)/combustion/reactingFoam \
-I$(LIB_SRC)/finiteVolume/lnInclude \
-I$(LIB_SRC)/meshTools/lnInclude \
-I$(LIB_SRC)/sampling/lnInclude \
-I$(LIB_SRC)/TurbulenceModels/turbulenceModels/lnInclude \
-I$(LIB_SRC)/TurbulenceModels/compressible/lnInclude \
-I$(LIB_SRC)/thermophysicalModels/specie/lnInclude \
-I$(LIB_SRC)/thermophysicalModels/reactionThermo/lnInclude \
-I$(LIB_SRC)/transportModels/compressible/lnInclude \
-I$(LIB_SRC)/thermophysicalModels/basic/lnInclude \
-I$(LIB_SRC)/thermophysicalModels/chemistryModel/lnInclude \
-I$(LIB_SRC)/ODE/lnInclude \
-I$(LIB_SRC)/combustionModels/lnInclude
EXE_LIBS = \
-lfiniteVolume \
-lfvOptions \
-lmeshTools \
-lsampling \
-lturbulenceModels \
-lcompressibleTurbulenceModels \
-lreactionThermophysicalModels \
-lspecie \
-lcompressibleTransportModels \
-lfluidThermophysicalModels \
-lchemistryModel \
-lODE \
-lcombustionModels
MRF.correctBoundaryVelocity(U);
fvVectorMatrix UEqn
(
fvm::ddt(rho, U) + fvm::div(phi, U)
+ MRF.DDt(rho, U)
+ turbulence->divDevRhoReff(U)
==
fvOptions(rho, U)
);
UEqn.relax();
fvOptions.constrain(UEqn);
if (pimple.momentumPredictor())
{
solve
(
UEqn
==
fvc::reconstruct
(
(
- ghf*fvc::snGrad(rho)
- fvc::snGrad(p_rgh)
)*mesh.magSf()
)
);
fvOptions.correct(U);
K = 0.5*magSqr(U);
}
const volScalarField& psi = thermo.psi();
const volScalarField& T = thermo.T();
const label inertIndex(composition.species()[inertSpecie]);
#include "createRDeltaT.H"
Info<< "Reading thermophysical properties\n" << endl;
autoPtr<rhoReactionThermo> pThermo(rhoReactionThermo::New(mesh));
rhoReactionThermo& thermo = pThermo();
thermo.validate(args.executable(), "h", "e");
basicSpecieMixture& composition = thermo.composition();
PtrList<volScalarField>& Y = composition.Y();
const word inertSpecie(thermo.get<word>("inertSpecie"));
if (!composition.species().found(inertSpecie))
{
FatalIOErrorIn(args.executable().c_str(), thermo)
<< "Inert specie " << inertSpecie << " not found in available species "
<< composition.species()
<< exit(FatalIOError);
}
volScalarField rho
(
IOobject
(
"rho",
runTime.timeName(),
mesh
),
thermo.rho()
);
Info<< "Reading field U\n" << endl;
volVectorField U
(
IOobject
(
"U",
runTime.timeName(),
mesh,
IOobject::MUST_READ,
IOobject::AUTO_WRITE
),
mesh
);
volScalarField& p = thermo.p();
#include "compressibleCreatePhi.H"
mesh.setFluxRequired(p.name());
Info << "Creating turbulence model.\n" << nl;
autoPtr<compressible::turbulenceModel> turbulence
(
compressible::turbulenceModel::New
(
rho,
U,
phi,
thermo
)
);
Info<< "Creating reaction model\n" << endl;
autoPtr<CombustionModel<rhoReactionThermo>> reaction
(
CombustionModel<rhoReactionThermo>::New(thermo, turbulence())
);
#include "readGravitationalAcceleration.H"
#include "readhRef.H"
#include "gh.H"
Info<< "Reading field p_rgh\n" << endl;
volScalarField p_rgh
(
IOobject
(
"p_rgh",
runTime.timeName(),
mesh,
IOobject::MUST_READ,
IOobject::AUTO_WRITE
),
mesh
);
// Force p_rgh to be consistent with p
p_rgh = p - rho*gh;
multivariateSurfaceInterpolationScheme<scalar>::fieldTable fields;
forAll(Y, i)
{
fields.add(Y[i]);
}
fields.add(thermo.he());
volScalarField Qdot
(
IOobject
(
"Qdot",
runTime.timeName(),
mesh,
IOobject::READ_IF_PRESENT,
IOobject::AUTO_WRITE
),
mesh,
dimensionedScalar(dimEnergy/dimVolume/dimTime, Zero)
);
#include "createDpdt.H"
#include "createK.H"
#include "createMRF.H"
#include "createFvOptions.H"
rho = thermo.rho();
// Thermodynamic density needs to be updated by psi*d(p) after the
// pressure solution
const volScalarField psip0(psi*p);
volScalarField rAU(1.0/UEqn.A());
surfaceScalarField rhorAUf("rhorAUf", fvc::interpolate(rho*rAU));
volVectorField HbyA(constrainHbyA(rAU*UEqn.H(), U, p));
surfaceScalarField phig(-rhorAUf*ghf*fvc::snGrad(rho)*mesh.magSf());
surfaceScalarField phiHbyA
(
"phiHbyA",
(
fvc::flux(rho*HbyA)
+ MRF.zeroFilter(rhorAUf*fvc::ddtCorr(rho, U, phi))
)
+ phig
);
MRF.makeRelative(fvc::interpolate(rho), phiHbyA);
// Update the pressure BCs to ensure flux consistency
constrainPressure(p_rgh, rho, U, phiHbyA, rhorAUf, MRF);
fvScalarMatrix p_rghDDtEqn
(
fvc::ddt(rho) + psi*correction(fvm::ddt(p_rgh))
+ fvc::div(phiHbyA)
==
fvOptions(psi, p_rgh, rho.name())
);
while (pimple.correctNonOrthogonal())
{
fvScalarMatrix p_rghEqn
(
p_rghDDtEqn
- fvm::laplacian(rhorAUf, p_rgh)
);
p_rghEqn.solve(mesh.solver(p_rgh.select(pimple.finalInnerIter())));
if (pimple.finalNonOrthogonalIter())
{
// Calculate the conservative fluxes
phi = phiHbyA + p_rghEqn.flux();
// Explicitly relax pressure for momentum corrector
p_rgh.relax();
// Correct the momentum source with the pressure gradient flux
// calculated from the relaxed pressure
U = HbyA + rAU*fvc::reconstruct((phig + p_rghEqn.flux())/rhorAUf);
U.correctBoundaryConditions();
fvOptions.correct(U);
K = 0.5*magSqr(U);
}
}
p = p_rgh + rho*gh;
// Thermodynamic density update
thermo.correctRho(psi*p - psip0);
if (thermo.dpdt())
{
dpdt = fvc::ddt(p);
}
#include "rhoEqn.H"
#include "compressibleContinuityErrs.H"
/*---------------------------------------------------------------------------*\
========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration |
\\ / A nd | www.openfoam.com
\\/ M anipulation |
-------------------------------------------------------------------------------
Copyright (C) 2012-2017 OpenFOAM Foundation
-------------------------------------------------------------------------------
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/>.
Application
rhoReactingBuoyantFoam
Group
grpCombustionSolvers
Description
Solver for combustion with chemical reactions using a density-based
thermodynamics package with enhanced buoyancy treatment.
\*---------------------------------------------------------------------------*/
#include "fvCFD.H"
#include "rhoReactionThermo.H"
#include "CombustionModel.H"
#include "turbulentFluidThermoModel.H"
#include "multivariateScheme.H"
#include "pimpleControl.H"
#include "fvOptions.H"
#include "localEulerDdtScheme.H"
#include "fvcSmooth.H"
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
int main(int argc, char *argv[])
{
argList::addNote
(
"Solver for combustion with chemical reactions using density-based"
" thermodynamics package,"
" with enhanced buoyancy treatment."
);
#include "postProcess.H"
#include "addCheckCaseOptions.H"
#include "setRootCaseLists.H"
#include "createTime.H"
#include "createMesh.H"
#include "createControl.H"
#include "createTimeControls.H"
#include "initContinuityErrs.H"
#include "createFields.H"
#include "createFieldRefs.H"
turbulence->validate();
if (!LTS)
{
#include "compressibleCourantNo.H"
#include "setInitialDeltaT.H"
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
Info<< "\nStarting time loop\n" << endl;
while (runTime.run())
{
#include "readTimeControls.H"
if (LTS)
{
#include "setRDeltaT.H"
}
else
{
#include "compressibleCourantNo.H"
#include "setDeltaT.H"
}
++runTime;
Info<< "Time = " << runTime.timeName() << nl << endl;
#include "rhoEqn.H"
// --- Pressure-velocity PIMPLE corrector loop
while (pimple.loop())
{
#include "UEqn.H"
#include "YEqn.H"
#include "EEqn.H"
// --- Pressure corrector loop
while (pimple.correct())
{
#include "pEqn.H"
}
if (pimple.turbCorr())
{
turbulence->correct();
}
}
rho = thermo.rho();
runTime.write();
runTime.printExecutionTime(Info);
}
Info<< "End\n" << endl;
return 0;
}
// ************************************************************************* //
rhoReactingFoam.C
EXE = $(FOAM_APPBIN)/rhoReactingFoam
EXE_INC = \
-I$(FOAM_SOLVERS)/combustion/reactingFoam \
-I$(LIB_SRC)/finiteVolume/lnInclude \
-I$(LIB_SRC)/meshTools/lnInclude \
-I$(LIB_SRC)/sampling/lnInclude \
-I$(LIB_SRC)/TurbulenceModels/turbulenceModels/lnInclude \
-I$(LIB_SRC)/TurbulenceModels/compressible/lnInclude \
-I$(LIB_SRC)/thermophysicalModels/specie/lnInclude \
-I$(LIB_SRC)/thermophysicalModels/reactionThermo/lnInclude \
-I$(LIB_SRC)/transportModels/compressible/lnInclude \
-I$(LIB_SRC)/thermophysicalModels/basic/lnInclude \
-I$(LIB_SRC)/thermophysicalModels/chemistryModel/lnInclude \
-I$(LIB_SRC)/ODE/lnInclude \
-I$(LIB_SRC)/combustionModels/lnInclude
EXE_LIBS = \
-lfiniteVolume \
-lfvOptions \
-lmeshTools \
-lsampling \
-lturbulenceModels \
-lcompressibleTurbulenceModels \
-lreactionThermophysicalModels \
-lspecie \
-lcompressibleTransportModels \
-lfluidThermophysicalModels \
-lchemistryModel \
-lODE \
-lcombustionModels
const volScalarField& psi = thermo.psi();
const volScalarField& T = thermo.T();
const label inertIndex(composition.species()[inertSpecie]);
#include "createRDeltaT.H"
Info<< "Reading thermophysical properties\n" << endl;
autoPtr<rhoReactionThermo> pThermo(rhoReactionThermo::New(mesh));
rhoReactionThermo& thermo = pThermo();
thermo.validate(args.executable(), "h", "e");
basicSpecieMixture& composition = thermo.composition();
PtrList<volScalarField>& Y = composition.Y();
const word inertSpecie(thermo.get<word>("inertSpecie"));
if (!composition.species().found(inertSpecie))
{
FatalIOErrorIn(args.executable().c_str(), thermo)
<< "Inert specie " << inertSpecie << " not found in available species "
<< composition.species()
<< exit(FatalIOError);
}
volScalarField rho
(
IOobject
(
"rho",
runTime.timeName(),
mesh
),
thermo.rho()
);
Info<< "Reading field U\n" << endl;
volVectorField U
(
IOobject
(
"U",
runTime.timeName(),
mesh,
IOobject::MUST_READ,
IOobject::AUTO_WRITE
),
mesh
);
volScalarField& p = thermo.p();
#include "compressibleCreatePhi.H"
pressureControl pressureControl(p, rho, pimple.dict(), false);
mesh.setFluxRequired(p.name());
Info << "Creating turbulence model.\n" << nl;
autoPtr<compressible::turbulenceModel> turbulence
(
compressible::turbulenceModel::New
(
rho,
U,
phi,
thermo
)
);
Info<< "Creating reaction model\n" << endl;
autoPtr<CombustionModel<rhoReactionThermo>> reaction
(
CombustionModel<rhoReactionThermo>::New(thermo, turbulence())
);
multivariateSurfaceInterpolationScheme<scalar>::fieldTable fields;
forAll(Y, i)
{
fields.add(Y[i]);
}
fields.add(thermo.he());
volScalarField Qdot
(
IOobject
(
"Qdot",
runTime.timeName(),
mesh,
IOobject::READ_IF_PRESENT,
IOobject::AUTO_WRITE
),
mesh,
dimensionedScalar(dimEnergy/dimVolume/dimTime, Zero)
);
#include "createDpdt.H"
#include "createK.H"
#include "createMRF.H"
const dimensionedScalar rhoMax("rhoMax", dimDensity, GREAT, pimple.dict());
const dimensionedScalar rhoMin("rhoMin", dimDensity, Zero, pimple.dict());
#include "createFvOptions.H"
/*---------------------------------------------------------------------------*\
========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration |
\\ / A nd | www.openfoam.com
\\/ M anipulation |
-------------------------------------------------------------------------------
Copyright (C) 2011-2017 OpenFOAM Foundation
-------------------------------------------------------------------------------
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/>.
Application
rhoReactingFoam
Group
grpCombustionSolvers
Description
Solver for combustion with chemical reactions using density-based
thermodynamics package.
\*---------------------------------------------------------------------------*/
#include "fvCFD.H"
#include "rhoReactionThermo.H"
#include "CombustionModel.H"
#include "turbulentFluidThermoModel.H"
#include "multivariateScheme.H"
#include "pimpleControl.H"
#include "pressureControl.H"
#include "fvOptions.H"
#include "localEulerDdtScheme.H"
#include "fvcSmooth.H"
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
int main(int argc, char *argv[])
{
argList::addNote
(
"Solver for combustion with chemical reactions using density-based"
" thermodynamics package."
);
#include "postProcess.H"
#include "addCheckCaseOptions.H"
#include "setRootCaseLists.H"
#include "createTime.H"
#include "createMesh.H"
#include "createControl.H"
#include "initContinuityErrs.H"
#include "createFields.H"
#include "createFieldRefs.H"
#include "createRhoUfIfPresent.H"
#include "createTimeControls.H"
turbulence->validate();
if (!LTS)
{
#include "compressibleCourantNo.H"
#include "setInitialDeltaT.H"
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
Info<< "\nStarting time loop\n" << endl;
while (runTime.run())
{
#include "readTimeControls.H"
if (LTS)
{
#include "setRDeltaT.H"
}
else
{
#include "compressibleCourantNo.H"
#include "setDeltaT.H"
}
++runTime;
Info<< "Time = " << runTime.timeName() << nl << endl;
#include "rhoEqn.H"
// --- Pressure-velocity PIMPLE corrector loop
while (pimple.loop())
{
#include "UEqn.H"
#include "YEqn.H"
#include "EEqn.H"
// --- Pressure corrector loop
while (pimple.correct())
{
if (pimple.consistent())
{
#include "../../../compressible/rhoPimpleFoam/pcEqn.H"
}
else
{
#include "../../../compressible/rhoPimpleFoam/pEqn.H"
}
}
if (pimple.turbCorr())
{
turbulence->correct();
}
}
rho = thermo.rho();
runTime.write();
runTime.printExecutionTime(Info);
}
Info<< "End\n" << endl;
return 0;
}
// ************************************************************************* //
/*---------------------------------------------------------------------------*\
========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration |
\\ / A nd | www.openfoam.com
\\/ M anipulation |
-------------------------------------------------------------------------------
Copyright (C) 2013-2016 OpenFOAM Foundation
Copyright (C) 2020 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 <http://www.gnu.org/licenses/>.
\*---------------------------------------------------------------------------*/
{
volScalarField& rDeltaT = trDeltaT.ref();
const dictionary& pimpleDict = pimple.dict();
// Maximum flow Courant number
scalar maxCo(pimpleDict.get<scalar>("maxCo"));
// Maximum time scale
scalar maxDeltaT(pimpleDict.getOrDefault<scalar>("maxDeltaT", GREAT));
// Smoothing parameter (0-1) when smoothing iterations > 0
scalar rDeltaTSmoothingCoeff
(
pimpleDict.getOrDefault<scalar>("rDeltaTSmoothingCoeff", 0.1)
);
// Damping coefficient (1-0)
scalar rDeltaTDampingCoeff
(
pimpleDict.getOrDefault<scalar>("rDeltaTDampingCoeff", 1.0)
);
// Maximum change in cell temperature per iteration
// (relative to previous value)
scalar alphaTemp(pimpleDict.getOrDefault<scalar>("alphaTemp", 0.05));
// Maximum change in cell concentration per iteration
// (relative to reference value)
scalar alphaY(pimpleDict.getOrDefault<scalar>("alphaY", 1.0));
Info<< "Time scales min/max:" << endl;
// Cache old reciprocal time scale field
volScalarField rDeltaT0("rDeltaT0", rDeltaT);
// Flow time scale
{
rDeltaT.ref() =
(
fvc::surfaceSum(mag(phi))()()
/((2*maxCo)*mesh.V()*rho())
);
// Limit the largest time scale
rDeltaT.max(1/maxDeltaT);
Info<< " Flow = "
<< 1/gMax(rDeltaT.primitiveField()) << ", "
<< 1/gMin(rDeltaT.primitiveField()) << endl;
}
// Heat release rate time scale
if (alphaTemp < 1)
{
volScalarField::Internal rDeltaTT
(
mag(Qdot)/(alphaTemp*rho*thermo.Cp()*T)
);
Info<< " Temperature = "
<< 1/(gMax(rDeltaTT.field()) + VSMALL) << ", "
<< 1/(gMin(rDeltaTT.field()) + VSMALL) << endl;
rDeltaT.ref() = max(rDeltaT(), rDeltaTT);
}
// Reaction rate time scale
if (alphaY < 1)
{
dictionary Yref(pimpleDict.subDict("Yref"));
volScalarField::Internal rDeltaTY
(
IOobject
(
"rDeltaTY",
runTime.timeName(),
mesh
),
mesh,
dimensionedScalar(rDeltaT.dimensions(), Zero)
);
bool foundY = false;
forAll(Y, i)
{
if (i != inertIndex && composition.active(i))
{
volScalarField& Yi = Y[i];
if (Yref.found(Yi.name()))
{
foundY = true;
const scalar Yrefi = Yref.get<scalar>(Yi.name());
rDeltaTY.field() = max
(
mag
(
reaction->R(Yi)().source()
/((Yrefi*alphaY)*(rho*mesh.V()))
),
rDeltaTY
);
}
}
}
if (foundY)
{
Info<< " Composition = "
<< 1/(gMax(rDeltaTY.field()) + VSMALL) << ", "
<< 1/(gMin(rDeltaTY.field()) + VSMALL) << endl;
rDeltaT.ref() = max(rDeltaT(), rDeltaTY);
}
else
{
IOWarningIn(args.executable().c_str(), Yref)
<< "Cannot find any active species in Yref " << Yref
<< endl;
}
}
// Update tho boundary values of the reciprocal time-step
rDeltaT.correctBoundaryConditions();
// Spatially smooth the time scale field
if (rDeltaTSmoothingCoeff < 1)
{
fvc::smooth(rDeltaT, rDeltaTSmoothingCoeff);
}
// Limit rate of change of time scale
// - reduce as much as required
// - only increase at a fraction of old time scale
if
(
rDeltaTDampingCoeff < 1
&& runTime.timeIndex() > runTime.startTimeIndex() + 1
)
{
rDeltaT = max
(
rDeltaT,
(scalar(1) - rDeltaTDampingCoeff)*rDeltaT0
);
}
// Update tho boundary values of the reciprocal time-step
rDeltaT.correctBoundaryConditions();
Info<< " Overall = "
<< 1/gMax(rDeltaT.primitiveField())
<< ", " << 1/gMin(rDeltaT.primitiveField()) << endl;
}
// ************************************************************************* //
/*---------------------------------------------------------------------------*\
========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration |
\\ / A nd | www.openfoam.com
\\/ M anipulation |
-------------------------------------------------------------------------------
Copyright (C) 2015 OpenFOAM Foundation
-------------------------------------------------------------------------------
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/>.
\defgroup grpCompressibleSolvers Compressible flow solvers
@{
\ingroup grpSolvers
This group contains compressible flow solvers.
@}
\*---------------------------------------------------------------------------*/
#!/bin/sh
cd "${0%/*}" || exit # Run from this directory
#------------------------------------------------------------------------------
wclean libso BCs
wclean
#------------------------------------------------------------------------------
#!/bin/sh
cd "${0%/*}" || exit # Run from this directory
. ${WM_PROJECT_DIR:?}/wmake/scripts/AllwmakeParseArguments
#------------------------------------------------------------------------------
(
wmake $targetType BCs \
&& wmake $targetType
)
#------------------------------------------------------------------------------
U/maxwellSlipUFvPatchVectorField.C
T/smoluchowskiJumpTFvPatchScalarField.C
rho/fixedRhoFvPatchScalarField.C
LIB = $(FOAM_LIBBIN)/librhoCentralFoam
EXE_INC = \
-I$(LIB_SRC)/finiteVolume/lnInclude \
-I$(LIB_SRC)/transportModels/compressible/lnInclude \
-I$(LIB_SRC)/thermophysicalModels/basic/lnInclude \
-I$(LIB_SRC)/thermophysicalModels/specie/lnInclude
LIB_LIBS = \
-lfiniteVolume \
-lcompressibleTransportModels \
-lfluidThermophysicalModels \
-lspecie
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