/*---------------------------------------------------------------------------*\
========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration |
\\ / A nd | www.openfoam.com
\\/ M anipulation |
-------------------------------------------------------------------------------
Copyright (C) 2018-2021 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 .
\*---------------------------------------------------------------------------*/
#include "Bromley.H"
#include "addToRunTimeSelectionTable.H"
#include "uniformDimensionedFields.H"
#include "constants.H"
using namespace Foam::constant;
// * * * * * * * * * * * * * * Static Data Members * * * * * * * * * * * * * //
namespace Foam
{
namespace wallBoilingModels
{
namespace filmBoilingModels
{
defineTypeNameAndDebug(Bromley, 0);
addToRunTimeSelectionTable
(
filmBoilingModel,
Bromley,
dictionary
);
}
}
}
// * * * * * * * * * * * * * * * * Constructors * * * * * * * * * * * * * * //
Foam::wallBoilingModels::filmBoilingModels::Bromley::Bromley
(
const dictionary& dict
)
:
filmBoilingModel(),
Cn_(dict.getOrDefault("Cn", 0.62)),
emissivity_(dict.getOrDefault("emissivity", 1)),
L_(dict.get("L"))
{}
// * * * * * * * * * * * * * * * Member Functions * * * * * * * * * * * * * //
Foam::tmp
Foam::wallBoilingModels::filmBoilingModels::Bromley::htcFilmBoil
(
const phaseModel& liquid,
const phaseModel& vapor,
const label patchi,
const scalarField& Tl,
const scalarField& Tsatw,
const scalarField& L
) const
{
const fvPatchScalarField& Tw =
liquid.thermo().T().boundaryField()[patchi];
const auto& g =
liquid.mesh().time().lookupObject("g");
const labelUList& cells = liquid.mesh().boundary()[patchi].faceCells();
const scalarField& pw = liquid.thermo().p().boundaryField()[patchi];
tmp trhoVapor = vapor.thermo().rhoEoS(pw, Tsatw, cells);
const scalarField& rhoVapor = trhoVapor.ref();
tmp trhoLiq = liquid.thermo().rhoEoS(pw, Tsatw, cells);
const scalarField& rhoLiq = trhoLiq.ref();
const scalarField kappaVapor(vapor.kappa(patchi));
tmp tCp = vapor.thermo().Cp(pw, Tsatw, cells);
const scalarField& CpVapor = tCp();
const scalarField muVapor(vapor.mu(patchi));
const scalarField htcRad
(
emissivity_*physicoChemical::sigma.value()*(pow4(Tw) - pow4(Tsatw))
/ max((Tw - Tsatw), scalar(1e-4))
);
return
Cn_*pow025
(
pow3(kappaVapor)
*rhoVapor*(rhoLiq - rhoVapor)*mag(g.value())
*(L + scalar(0.4)*CpVapor*max((Tw-Tsatw), scalar(0)))
/(L_*muVapor*max((Tw-Tsatw), scalar(1e-4)))
) + scalar(0.75)*htcRad;
}
void Foam::wallBoilingModels::filmBoilingModels::Bromley::write
(
Ostream& os
) const
{
filmBoilingModel::write(os);
os.writeEntry("Cn", Cn_);
os.writeEntry("L", L_);
os.writeEntry("emissivity", emissivity_);
}
// ************************************************************************* //