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/*---------------------------------------------------------------------------*\
========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration | Website: https://openfoam.org
\\ / A nd | Copyright (C) 2011-2026 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 "FSD.H"
#include "addToRunTimeSelectionTable.H"
#include "LESModel.H"
#include "fviGrad.H"
#include "fviDiv.H"
#include "addToRunTimeSelectionTable.H"
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
namespace Foam
{
namespace reactionModels
{
defineTypeNameAndDebug(FSD, 0);
addToRunTimeSelectionTable(reactionModel, FSD, dictionary);
}
}
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
Foam::reactionModels::FSD::FSD
(
const word& modelType,
const fluidMulticomponentThermo& thermo,
const compressibleMomentumTransportModel& turb,
const word& reactionProperties
)
:
singleStepReaction
(
modelType,
thermo,
turb,
reactionProperties
),
reactionRateFlameArea_
(
reactionRateFlameArea::New
(
this->coeffs(),
this->mesh(),
*this
)
),
ft_
(
IOobject
(
this->thermo().phasePropertyName("ft"),
this->mesh().time().name(),
this->mesh(),
IOobject::NO_READ,
IOobject::AUTO_WRITE
),
this->mesh(),
dimensionedScalar(dimless, 0)
),
YFuelFuelStream_(dimensionedScalar(dimless, 1.0)),
YO2OxiStream_(dimensionedScalar(dimless, 0.23)),
Cv_(this->coeffs().template lookup<scalar>("Cv")),
C_(5),
ftMin_(0),
ftMax_(1),
ftDim_(300),
ftVarMin_(this->coeffs().template lookup<scalar>("ftVarMin"))
{}
// * * * * * * * * * * * * * * * * Destructor * * * * * * * * * * * * * * * //
Foam::reactionModels::FSD::~FSD()
{}
// * * * * * * * * * * * * * * Member Functions * * * * * * * * * * * * * * //
void Foam::reactionModels::FSD::calculateSourceNorm()
{
this->fresCorrect();
const label fuelI = this->fuelIndex();
const volScalarField& YFuel = this->thermo().Y()[fuelI];
const volScalarField& YO2 = this->thermo().Y("O2");
const dimensionedScalar s = this->s();
ft_ =
(s*YFuel - (YO2 - YO2OxiStream_))/(s*YFuelFuelStream_ + YO2OxiStream_);
volInternalVectorField nft(fvi::grad(ft_));
volInternalScalarField mgft(mag(nft));
const volInternalScalarField cAux(scalar(1) - ft_());
const dimensionedScalar dMgft = 1e-3*
sum(ft_()*cAux*mgft*this->mesh().V())
/(
sum(ft_()*cAux*this->mesh().V())
+ dimensionedScalar(dimVolume, rootVSmall)
)
+ dimensionedScalar(mgft.dimensions(), small);
mgft += dMgft;
nft /= mgft;
const volVectorField& U = YO2.db().lookupObject<volVectorField>("U");
const volInternalScalarField sigma
(
(nft & nft)*fvi::div(U) - (nft & fvi::grad(U) & nft)
);
reactionRateFlameArea_->correct(sigma);
const volScalarField& omegaFuel = reactionRateFlameArea_->omega();
const scalar ftStoich =
YO2OxiStream_.value()
/(
s.value()*YFuelFuelStream_.value() + YO2OxiStream_.value()
);
tmp<volScalarField> tPc
(
volScalarField::New
(
this->thermo().phasePropertyName("Pc"),
U.mesh(),
dimensionedScalar(dimless, 0)
)
);
volScalarField& pc = tPc.ref();
tmp<volScalarField> tomegaFuel
(
volScalarField::New
(
this->thermo().phasePropertyName("omegaFuelBar"),
U.mesh(),
dimensionedScalar(omegaFuel.dimensions(), 0)
)
);
volScalarField& omegaFuelBar = tomegaFuel.ref();
// Calculation of the mixture fraction variance (ftVar)
const compressible::LESModel& lesModel =
YO2.db().lookupObject<compressible::LESModel>
(
momentumTransportModel::typeName
);
const volInternalScalarField& delta = lesModel.delta();
const volInternalScalarField ftVar(Cv_*sqr(delta)*sqr(mgft));
// Thickened flame (average flame thickness for counterflow configuration
// is 1.5 mm)
const volScalarField deltaF
(
lesModel.delta()/dimensionedScalar(dimensions::length, 1.5e-3)
);
// Linear correlation between delta and flame thickness
const volScalarField omegaF(max(deltaF*(4.0/3.0) + (2.0/3.0), scalar(1)));
const scalar deltaFt = 1/ftDim_;
forAll(ft_, celli)
{
if (ft_[celli] > ftMin_ && ft_[celli] < ftMax_)
{
const scalar ftCell = ft_[celli];
if (ftVar[celli] > ftVarMin_) // sub-grid beta pdf of ft_
{
const scalar ftVarc = ftVar[celli];
const scalar a =
max(ftCell*(ftCell*(1 - ftCell)/ftVarc - 1), 0);
const scalar b = max(a/ftCell - a, 0);
for (int i=1; i<ftDim_; i++)
{
const scalar ft = i*deltaFt;
pc[celli] += pow(ft, a - 1)*pow(1 - ft, b - 1)*deltaFt;
}
for (int i=1; i<ftDim_; i++)
{
const scalar ft = i*deltaFt;
omegaFuelBar[celli] +=
omegaFuel[celli]/omegaF[celli]
*exp
(
-sqr(ft - ftStoich)
/(2*sqr(0.01*omegaF[celli]))
)
*pow(ft, a - 1)
*pow(1 - ft, b - 1)
*deltaFt;
}
omegaFuelBar[celli] /= max(pc[celli], 1e-4);
}
else
{
omegaFuelBar[celli] =
omegaFuel[celli]/omegaF[celli]
*exp(-sqr(ftCell - ftStoich)/(2*sqr(0.01*omegaF[celli])));
}
}
else
{
omegaFuelBar[celli] = 0;
}
}
// Reaction progress variable, c
List<label> productsIndex(2, label(-1));
{
label i = 0;
forAll(this->specieProd(), specieI)
{
if (this->specieProd()[specieI] < 0)
{
productsIndex[i] = specieI;
i++;
}
}
}
// Flamelet probability of the progress c based on IFC (reuse pc)
scalar YprodTotal = 0;
forAll(productsIndex, j)
{
YprodTotal += this->Yprod0()[productsIndex[j]];
}
forAll(ft_, celli)
{
if (ft_[celli] < ftStoich)
{
pc[celli] = ft_[celli]*(YprodTotal/ftStoich);
}
else
{
pc[celli] = (1 - ft_[celli])*(YprodTotal/(1 - ftStoich));
}
}
tmp<volScalarField> tproducts
(
volScalarField::New
(
this->thermo().phasePropertyName("products"),
U.mesh(),
dimensionedScalar(dimless, 0)
)
);
volScalarField& products = tproducts.ref();
forAll(productsIndex, j)
{
const label specieI = productsIndex[j];
const volScalarField& Yp = this->thermo().Y()[specieI];
products += Yp;
}
volScalarField c
(
max(scalar(1) - products/max(pc, scalar(1e-5)), scalar(0))
);
pc = min(C_*c, scalar(1));
const volScalarField fres(this->fres(fuelI));
this->wFuel_ = mgft*pc()*omegaFuelBar();
}
void Foam::reactionModels::FSD::correct()
{
this->wFuel_ = dimensionedScalar(dimensions::density/dimensions::time, 0);
calculateSourceNorm();
}
bool Foam::reactionModels::FSD::read()
{
if (singleStepReaction::read())
{
this->coeffs().lookup("Cv") >> Cv_ ;
this->coeffs().lookup("ftVarMin") >> ftVarMin_;
reactionRateFlameArea_->read(this->coeffs());
return true;
}
else
{
return false;
}
}
// ************************************************************************* //