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ENH: Updating wall boiling models for new rho and Cp functions

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This commit is contained in:
sergio
2021-12-10 09:58:09 +00:00
committed by Andrew Heather
parent f309319c06
commit 17657673b2
4 changed files with 46 additions and 20 deletions
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12
src/phaseSystemModels/reactingEuler/multiphaseSystem/derivedFvPatchFields/wallBoilingSubModels/CHFModels/Zuber/Zuber.C
View File

@ -5,7 +5,7 @@
\\ / A nd | www.openfoam.com
\\/ M anipulation |
-------------------------------------------------------------------------------
Copyright (C) 2018-2020 OpenCFD Ltd
Copyright (C) 2018-2021 OpenCFD Ltd
-------------------------------------------------------------------------------
License
This file is part of OpenFOAM.
@ -85,9 +85,15 @@ Foam::wallBoilingModels::CHFModels::Zuber::CHF
const uniformDimensionedVectorField& g =
liquid.mesh().time().lookupObject<uniformDimensionedVectorField>("g");
const scalarField rhoVapor(vapor.thermo().rho(patchi));
const scalarField rhoLiq(liquid.thermo().rho(patchi));
const labelUList& cells = liquid.mesh().boundary()[patchi].faceCells();
const scalarField& pw = liquid.thermo().p().boundaryField()[patchi];
tmp<scalarField> trhoVapor = vapor.thermo().rhoEoS(Tsatw, pw, cells);
const scalarField& rhoVapor = trhoVapor.ref();
tmp<scalarField> trhoLiq = liquid.thermo().rhoEoS(Tsatw, pw, cells);
const scalarField& rhoLiq = trhoLiq.ref();
const phasePairKey pair(liquid.name(), vapor.name());
const scalarField sigma
(

15
src/phaseSystemModels/reactingEuler/multiphaseSystem/derivedFvPatchFields/wallBoilingSubModels/CHFSubCoolModels/HuaXu/HuaXu.C
View File

@ -5,7 +5,7 @@
\\ / A nd | www.openfoam.com
\\/ M anipulation |
-------------------------------------------------------------------------------
Copyright (C) 2018-2020 OpenCFD Ltd
Copyright (C) 2018-2021 OpenCFD Ltd
-------------------------------------------------------------------------------
License
This file is part of OpenFOAM.
@ -87,8 +87,17 @@ Foam::wallBoilingModels::CHFModels::HuaXu::CHFSubCool
const scalarField alphaLiq(liquid.alpha(patchi));
const scalarField rhoVapor(vapor.thermo().rho(patchi));
const scalarField rhoLiq(liquid.thermo().rho(patchi));
const labelUList& cells = liquid.mesh().boundary()[patchi].faceCells();
const scalarField& pw = liquid.thermo().p().boundaryField()[patchi];
tmp<scalarField> trhoVapor = vapor.thermo().rhoEoS(Tsatw, pw, cells);
const scalarField& rhoVapor = trhoVapor.ref();
tmp<scalarField> trhoLiq = liquid.thermo().rhoEoS(Tsatw, pw, cells);
const scalarField& rhoLiq = trhoLiq.ref();
tmp<volScalarField> tCp = liquid.thermo().Cp();
const volScalarField& Cp = tCp();
const fvPatchScalarField& Cpw = Cp.boundaryField()[patchi];

17
src/phaseSystemModels/reactingEuler/multiphaseSystem/derivedFvPatchFields/wallBoilingSubModels/MHFModels/Jeschar/Jeschar.C
View File

@ -5,7 +5,7 @@
\\ / A nd | www.openfoam.com
\\/ M anipulation |
-------------------------------------------------------------------------------
Copyright (C) 2018-2020 OpenCFD Ltd
Copyright (C) 2018-2021 OpenCFD Ltd
-------------------------------------------------------------------------------
License
This file is part of OpenFOAM.
@ -59,7 +59,7 @@ Foam::wallBoilingModels::CHFModels::Jeschar::Jeschar
)
:
MHFModel(),
Kmhf_(dict.getOrDefault<scalar>("Kmhf", 1))
Kmhf_(dict.getOrDefault<scalar>("Kmhf", 0.16))
{}
@ -85,8 +85,15 @@ Foam::wallBoilingModels::CHFModels::Jeschar::MHF
const uniformDimensionedVectorField& g =
liquid.mesh().time().lookupObject<uniformDimensionedVectorField>("g");
const scalarField rhoVapor(vapor.thermo().rho(patchi));
const scalarField rhoLiq(liquid.thermo().rho(patchi));
const labelUList& cells = liquid.mesh().boundary()[patchi].faceCells();
const scalarField& pw = liquid.thermo().p().boundaryField()[patchi];
tmp<scalarField> trhoVapor = vapor.thermo().rhoEoS(Tsatw, pw, cells);
const scalarField& rhoVapor = trhoVapor.ref();
tmp<scalarField> trhoLiq = liquid.thermo().rhoEoS(Tsatw, pw, cells);
const scalarField& rhoLiq = trhoLiq.ref();
const phasePairKey pair(liquid.name(), vapor.name());
const scalarField sigma
@ -95,7 +102,7 @@ Foam::wallBoilingModels::CHFModels::Jeschar::MHF
);
return
Kmhf_*0.09*rhoVapor*L
Kmhf_*rhoVapor*L
*(
pow(sigma/(mag(g.value())*(rhoLiq - rhoVapor)), 0.25)
* sqrt(mag(g.value())*(rhoLiq - rhoVapor)/(rhoLiq + rhoVapor))

22
src/phaseSystemModels/reactingEuler/multiphaseSystem/derivedFvPatchFields/wallBoilingSubModels/filmBoilingModels/Bromley/Bromley.C
View File

@ -5,7 +5,7 @@
\\ / A nd | www.openfoam.com
\\/ M anipulation |
-------------------------------------------------------------------------------
Copyright (C) 2018-2020 OpenCFD Ltd
Copyright (C) 2018-2021 OpenCFD Ltd
-------------------------------------------------------------------------------
License
This file is part of OpenFOAM.
@ -85,18 +85,23 @@ Foam::wallBoilingModels::filmBoilingModels::Bromley::htcFilmBoil
const scalarField& L
) const
{
const fvPatchScalarField& Tw =
liquid.thermo().T().boundaryField()[patchi];
const uniformDimensionedVectorField& g =
liquid.mesh().time().lookupObject<uniformDimensionedVectorField>("g");
const fvPatchScalarField& rhoVaporw
(
vapor.thermo().rho()().boundaryField()[patchi]
);
const labelUList& cells = liquid.mesh().boundary()[patchi].faceCells();
const scalarField& pw = liquid.thermo().p().boundaryField()[patchi];
tmp<scalarField> trhoVapor = vapor.thermo().rhoEoS(Tsatw, pw, cells);
const scalarField& rhoVapor = trhoVapor.ref();
tmp<scalarField> trhoLiq = liquid.thermo().rhoEoS(Tsatw, pw, cells);
const scalarField& rhoLiq = trhoLiq.ref();
const scalarField rhoLiq(liquid.thermo().rho(patchi));
const scalarField kappaVapor(vapor.kappa(patchi));
tmp<volScalarField> tCp = vapor.thermo().Cp();
@ -104,7 +109,6 @@ Foam::wallBoilingModels::filmBoilingModels::Bromley::htcFilmBoil
const scalarField& CpVapor = Cp.boundaryField()[patchi];
const scalarField muVapor(vapor.mu(patchi));
//const scalarField dbVapor(vapor.d()().boundaryField()[patchi]);
const scalarField htcRad
(
@ -116,7 +120,7 @@ Foam::wallBoilingModels::filmBoilingModels::Bromley::htcFilmBoil
Cn_*pow
(
pow3(kappaVapor)
*rhoVaporw*(rhoLiq - rhoVaporw)*mag(g.value())
*rhoVapor*(rhoLiq - rhoVapor)*mag(g.value())
*(L + 0.4*CpVapor*max((Tw-Tsatw), scalar(0)))
/(L_*muVapor*max((Tw-Tsatw), scalar(1e-4))),
0.25