waxSolventEvaporation.C

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    Copyright (C) 2017 OpenFOAM Foundation
    Copyright (C) 2020 OpenCFD Ltd.
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License
    This file is part of OpenFOAM.
 
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    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.
 
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    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
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#include "waxSolventEvaporation.H"
#include "addToRunTimeSelectionTable.H"
#include "thermoSingleLayer.H"
#include "zeroField.H"
 
#include "fvmDdt.H"
#include "fvmDiv.H"
#include "fvcDiv.H"
#include "fvmSup.H"
 
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
 
namespace Foam
{
namespace regionModels
{
namespace surfaceFilmModels
{
 
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
 
defineTypeNameAndDebug(waxSolventEvaporation, 0);
 
addToRunTimeSelectionTable
(
    phaseChangeModel,
    waxSolventEvaporation,
    dictionary
);
 
// * * * * * * * * * * * * Protected Member Functions  * * * * * * * * * * * //
 
scalar waxSolventEvaporation::Sh
(
    const scalar Re,
    const scalar Sc
) const
{
    if (Re < 5.0E+05)
    {
        return 0.664*sqrt(Re)*cbrt(Sc);
    }
    else
    {
        return 0.037*pow(Re, 0.8)*cbrt(Sc);
    }
}
 
 
// * * * * * * * * * * * * * * * * Constructors  * * * * * * * * * * * * * * //
 
waxSolventEvaporation::waxSolventEvaporation
(
    surfaceFilmRegionModel& film,
    const dictionary& dict
)
:
    phaseChangeModel(typeName, film, dict),
    Wwax_
    (
        IOobject
        (
            typeName + ":Wwax",
            film.regionMesh().time().constant(),
            film.regionMesh()
        ),
        coeffDict_.get<scalar>("Wwax")
    ),
    Wsolvent_
    (
        IOobject
        (
            typeName + ":Wsolvent",
            film.regionMesh().time().constant(),
            film.regionMesh()
        ),
        coeffDict_.get<scalar>("Wsolvent")
    ),
    Ysolvent0_
    (
        IOobject
        (
            typeName + ":Ysolvent0",
            film.regionMesh().time().constant(),
            film.regionMesh(),
            IOobject::MUST_READ,
            IOobject::NO_WRITE
        )
    ),
    Ysolvent_
    (
        IOobject
        (
            typeName + ":Ysolvent",
            film.regionMesh().time().timeName(),
            film.regionMesh(),
            IOobject::MUST_READ,
            IOobject::AUTO_WRITE
        ),
        film.regionMesh()
    ),
    deltaMin_(coeffDict_.get<scalar>("deltaMin")),
    L_(coeffDict_.get<scalar>("L")),
    TbFactor_(coeffDict_.getOrDefault<scalar>("TbFactor", 1.1)),
    YInfZero_(coeffDict_.getOrDefault("YInfZero", false)),
    activityCoeff_
    (
        Function1<scalar>::New("activityCoeff", coeffDict_, &film.regionMesh())
    )
{}
 
 
// * * * * * * * * * * * * * * * * Destructor  * * * * * * * * * * * * * * * //
 
waxSolventEvaporation::~waxSolventEvaporation()
{}
 
 
// * * * * * * * * * * * * * * Member Functions  * * * * * * * * * * * * * * //
 
template<class YInfType>
void waxSolventEvaporation::correctModel
(
    const scalar dt,
    scalarField& availableMass,
    scalarField& dMass,
    scalarField& dEnergy,
    YInfType YInf
)
{
    const thermoSingleLayer& film = filmType<thermoSingleLayer>();
 
    const volScalarField& delta = film.delta();
    const volScalarField& deltaRho = film.deltaRho();
    const surfaceScalarField& phi = film.phi();
 
    // Set local thermo properties
    const SLGThermo& thermo = film.thermo();
    const filmThermoModel& filmThermo = film.filmThermo();
    const label vapId = thermo.carrierId(filmThermo.name());
 
    // Retrieve fields from film model
    const scalarField& pInf = film.pPrimary();
    const scalarField& T = film.T();
    const scalarField& hs = film.hs();
    const scalarField& rho = film.rho();
    const scalarField& rhoInf = film.rhoPrimary();
    const scalarField& muInf = film.muPrimary();
    const scalarField& magSf = film.magSf();
    const vectorField dU(film.UPrimary() - film.Us());
    const scalarField limMass
    (
        max(scalar(0), availableMass - deltaMin_*rho*magSf)
    );
 
    // Molecular weight of vapour [kg/kmol]
    const scalar Wvap = thermo.carrier().W(vapId);
 
    const scalar Wwax = Wwax_.value();
    const scalar Wsolvent = Wsolvent_.value();
 
    volScalarField::Internal evapRateCoeff
    (
        IOobject
        (
            typeName + ":evapRateCoeff",
            film.regionMesh().time().timeName(),
            film.regionMesh(),
            IOobject::NO_READ,
            IOobject::NO_WRITE,
            false
        ),
        film.regionMesh(),
        dimensionedScalar(dimDensity*dimVelocity, Zero)
    );
 
    volScalarField::Internal evapRateInf
    (
        IOobject
        (
            typeName + ":evapRateInf",
            film.regionMesh().time().timeName(),
            film.regionMesh(),
            IOobject::NO_READ,
            IOobject::NO_WRITE,
            false
        ),
        film.regionMesh(),
        dimensionedScalar(dimDensity*dimVelocity, Zero)
    );
 
    bool filmPresent = false;
 
    forAll(dMass, celli)
    {
        if (delta[celli] > deltaMin_)
        {
            filmPresent = true;
 
            const scalar Ysolvent = Ysolvent_[celli];
 
            // Molefraction of solvent in liquid film
            const scalar Xsolvent
            (
                Ysolvent*Wsolvent/((1 - Ysolvent)*Wwax + Ysolvent*Wsolvent)
            );
 
            // Primary region density [kg/m3]
            const scalar rhoInfc = rhoInf[celli];
 
            // Cell pressure [Pa]
            const scalar pc = pInf[celli];
 
            // Calculate the boiling temperature
            const scalar Tb = filmThermo.Tb(pc);
 
            // Local temperature - impose lower limit of 200 K for stability
            const scalar Tloc = min(TbFactor_*Tb, max(200.0, T[celli]));
 
            const scalar pPartialCoeff
            (
                filmThermo.pv(pc, Tloc)*activityCoeff_->value(Xsolvent)
            );
 
            scalar XsCoeff = pPartialCoeff/pc;
 
            // Vapour phase mole fraction of solvent at interface
            scalar Xs = XsCoeff*Xsolvent;
 
            if (Xs > 1)
            {
                WarningInFunction
                    << "Solvent vapour pressure > ambient pressure"
                    << endl;
 
                XsCoeff /= Xs;
                Xs = 1;
            }
 
            // Vapour phase mass fraction of solvent at the interface
            const scalar YsCoeff
            (
                XsCoeff/(XsCoeff*Xsolvent*Wsolvent + (1 - Xs)*Wvap)
            );
 
            // Primary region viscosity [Pa.s]
            const scalar muInfc = muInf[celli];
 
            // Reynolds number
            const scalar Re = rhoInfc*mag(dU[celli])*L_/muInfc;
 
            // Vapour diffusivity [m2/s]
            const scalar Dab = filmThermo.D(pc, Tloc);
 
            // Schmidt number
            const scalar Sc = muInfc/(rhoInfc*(Dab + ROOTVSMALL));
 
            // Sherwood number
            const scalar Sh = this->Sh(Re, Sc);
 
            // Mass transfer coefficient [m/s]
            evapRateCoeff[celli] = rhoInfc*Sh*Dab/(L_ + ROOTVSMALL);
 
            // Solvent mass transfer
            const scalar dm
            (
                max
                (
                    dt*magSf[celli]
                   *evapRateCoeff[celli]*(YsCoeff*Ysolvent - YInf[celli]),
                    0
                )
            );
 
            if (dm > limMass[celli])
            {
                evapRateCoeff[celli] *= limMass[celli]/dm;
            }
 
            evapRateInf[celli] = evapRateCoeff[celli]*YInf[celli];
            evapRateCoeff[celli] *= YsCoeff;
 
            // hVap[celli] = filmThermo.hl(pc, Tloc);
        }
    }
 
    const dimensionedScalar deltaRho0Bydt
    (
        "deltaRho0",
        deltaRho.dimensions()/dimTime,
        ROOTVSMALL/dt
    );
 
    volScalarField::Internal impingementRate
    (
        max
        (
           -film.rhoSp()(),
            dimensionedScalar(film.rhoSp().dimensions(), Zero)
        )
    );
 
    if (filmPresent)
    {
        // Solve for the solvent mass fraction
        fvScalarMatrix YsolventEqn
        (
            fvm::ddt(deltaRho, Ysolvent_)
          + fvm::div(phi, Ysolvent_)
         ==
            deltaRho0Bydt*Ysolvent_()
 
          + evapRateInf
 
            // Include the effect of the impinging droplets
            // added with Ysolvent = Ysolvent0
          + impingementRate*Ysolvent0_
 
          - fvm::Sp
            (
                deltaRho0Bydt
              + evapRateCoeff
              + film.rhoSp()()
              + impingementRate,
                Ysolvent_
            )
        );
 
        YsolventEqn.relax();
        YsolventEqn.solve();
 
        Ysolvent_.min(1);
        Ysolvent_.max(0);
 
        scalarField dm
        (
            dt*magSf*rhoInf*(evapRateCoeff*Ysolvent_ + evapRateInf)
        );
 
        dMass += dm;
 
        // Heat is assumed to be removed by heat-transfer to the wall
        // so the energy remains unchanged by the phase-change.
        dEnergy += dm*hs;
 
        // Latent heat [J/kg]
        // dEnergy += dm*(hs[celli] + hVap);
    }
}
 
 
void waxSolventEvaporation::correctModel
(
    const scalar dt,
    scalarField& availableMass,
    scalarField& dMass,
    scalarField& dEnergy
)
{
    if (YInfZero_)
    {
        correctModel(dt, availableMass, dMass, dEnergy, zeroField());
    }
    else
    {
        const thermoSingleLayer& film = filmType<thermoSingleLayer>();
        const label vapId = film.thermo().carrierId(film.filmThermo().name());
        const scalarField& YInf = film.YPrimary()[vapId];
 
        correctModel(dt, availableMass, dMass, dEnergy, YInf);
    }
}
 
 
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
 
} // End namespace surfaceFilmModels
} // End namespace regionModels
} // End namespace Foam
 
// ************************************************************************* //