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synced 2025-11-28 03:28:01 +00:00
BUG: twoPhaseEulerFoam: removed multiple of the continuous phase fraction from force and heat transfer models
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@ -23,12 +23,11 @@ volScalarField dragCoeff(fluid.dragCoeff());
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+ phase1.turbulence().divDevReff(U1)
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==
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- fvm::Sp(dragCoeff/rho1, U1)
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- alpha1*alpha2/rho1
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*(
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- (
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liftForce
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+ wallLubricationForce
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+ turbulentDispersionForce
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)
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)/rho1
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- virtualMassCoeff/rho1
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*(
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fvm::ddt(U1)
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@ -50,12 +49,11 @@ volScalarField dragCoeff(fluid.dragCoeff());
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+ phase2.turbulence().divDevReff(U2)
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==
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- fvm::Sp(dragCoeff/rho2, U2)
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+ alpha1*alpha2/rho2
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*(
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+ (
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liftForce
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+ wallLubricationForce
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+ turbulentDispersionForce
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)
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)/rho2
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- virtualMassCoeff/rho2
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*(
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fvm::ddt(U2)
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@ -107,13 +107,11 @@ Foam::tmp<Foam::volScalarField> Foam::dragModel::K() const
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return
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0.75
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*CdRe()
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*max(pair_.dispersed(), residualAlpha_)
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*swarmCorrection_->Cs()
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*pair_.continuous().rho()
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*pair_.continuous().nu()
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/(
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max(pair_.continuous(), residualAlpha_)
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*sqr(pair_.dispersed().d())
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);
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/sqr(pair_.dispersed().d());
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}
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@ -64,7 +64,12 @@ Foam::heatTransferModels::RanzMarshall::K() const
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{
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volScalarField Nu(scalar(2) + 0.6*pair_.Re()*cbrt(pair_.Pr()));
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return 6.0*pair_.continuous().kappa()*Nu/sqr(pair_.dispersed().d());
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return
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6.0
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*max(pair_.dispersed(), residualAlpha_)
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*pair_.continuous().kappa()
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*Nu
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/sqr(pair_.dispersed().d());
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}
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@ -45,7 +45,8 @@ Foam::heatTransferModel::heatTransferModel
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const phasePair& pair
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)
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:
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pair_(pair)
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pair_(pair),
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residualAlpha_("residualAlpha", dimless, dict.lookup("residualAlpha"))
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{}
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@ -58,6 +58,9 @@ protected:
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//- Phase pair
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const phasePair& pair_;
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//- Residual phase fraction
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const dimensionedScalar residualAlpha_;
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public:
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@ -62,6 +62,7 @@ Foam::tmp<Foam::volVectorField> Foam::liftModel::F() const
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{
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return
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Cl()
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*pair_.dispersed()
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*pair_.continuous().rho()
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*(
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pair_.Ur() ^ fvc::curl(pair_.continuous().U())
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@ -85,6 +85,7 @@ Foam::turbulentDispersionModels::Gosman::F() const
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return
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- 0.75
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*drag.CdRe()
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*pair_.dispersed()
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*pair_.continuous().nu()
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*pair_.continuous().turbulence().nut()
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/(
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@ -75,6 +75,7 @@ F() const
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{
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return
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- Ctd_
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*pair_.dispersed()
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*pair_.continuous().rho()
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*pair_.continuous().turbulence().k()
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*fvc::grad(pair_.dispersed());
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@ -72,7 +72,7 @@ Foam::virtualMassModel::~virtualMassModel()
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Foam::tmp<Foam::volScalarField> Foam::virtualMassModel::K() const
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{
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return Cvm()*pair_.continuous().rho();
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return Cvm()*pair_.dispersed()*pair_.continuous().rho();
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}
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@ -79,6 +79,7 @@ Foam::tmp<Foam::volVectorField> Foam::wallLubricationModels::Antal::F() const
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dimensionedScalar("zero", dimless/dimLength, 0),
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Cw1_/pair_.dispersed().d() + Cw2_/yWall_
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)
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*pair_.dispersed()
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*pair_.continuous().rho()
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*magSqr(Ur - (Ur & nWall)*nWall)
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*nWall;
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@ -163,8 +163,6 @@ Foam::BlendedInterfacialModel<modelType>::K() const
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if (model_.valid() || model1In2_.valid() || model2In1_.valid())
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{
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x() *= max(pair_.phase1()*pair_.phase2(), blending_.residualAlpha());
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correctFixedFluxBCs(x());
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}
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@ -40,8 +40,6 @@ Foam::blendingMethod::blendingMethod
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(
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const dictionary& dict
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)
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:
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residualAlpha_("residualAlpha", dimless, dict.lookup("residualAlpha"))
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{}
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@ -51,12 +49,4 @@ Foam::blendingMethod::~blendingMethod()
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{}
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// * * * * * * * * * * * * * * Member Functions * * * * * * * * * * * * * * //
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const Foam::dimensionedScalar& Foam::blendingMethod::residualAlpha() const
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{
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return residualAlpha_;
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}
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// ************************************************************************* //
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@ -49,14 +49,6 @@ namespace Foam
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class blendingMethod
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{
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protected:
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// Protected data
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//- Residual phase fraction
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const dimensionedScalar residualAlpha_;
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public:
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//- Runtime type information
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@ -101,9 +93,6 @@ public:
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// Member Functions
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//- Residual phase fraction
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const dimensionedScalar& residualAlpha() const;
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//- Factor for first phase
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virtual tmp<volScalarField> f1
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(
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@ -41,7 +41,6 @@ blending
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default
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{
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type linear;
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residualAlpha 1e-6;
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maxFullyDispersedAlpha.air 0.3;
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maxPartlyDispersedAlpha.air 0.5;
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maxFullyDispersedAlpha.water 0.3;
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@ -126,11 +125,13 @@ heatTransfer
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(air in water)
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{
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type RanzMarshall;
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residualAlpha 1e-6;
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}
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(water in air)
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{
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type RanzMarshall;
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residualAlpha 1e-6;
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}
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);
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@ -41,7 +41,6 @@ blending
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default
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{
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type linear;
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residualAlpha 1e-6;
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maxFullyDispersedAlpha.air 0.3;
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maxPartlyDispersedAlpha.air 0.5;
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maxFullyDispersedAlpha.water 0.3;
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@ -126,11 +125,13 @@ heatTransfer
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(air in water)
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{
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type RanzMarshall;
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residualAlpha 1e-6;
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}
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(water in air)
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{
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type RanzMarshall;
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residualAlpha 1e-6;
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}
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);
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@ -42,7 +42,6 @@ blending
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default
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{
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type none;
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residualAlpha 1e-3;
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continuousPhase air;
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}
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}
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@ -72,11 +71,6 @@ drag
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virtualMass
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(
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(particles in air)
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{
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type constantCoefficient;
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Cvm 0;
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}
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);
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heatTransfer
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@ -84,6 +78,7 @@ heatTransfer
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(particles in air)
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{
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type RanzMarshall;
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residualAlpha 1e-3;
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}
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);
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@ -41,7 +41,6 @@ blending
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default
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{
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type linear;
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residualAlpha 1e-6;
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maxFullyDispersedAlpha.air 0.3;
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maxPartlyDispersedAlpha.air 0.5;
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maxFullyDispersedAlpha.water 0.3;
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@ -126,11 +125,13 @@ heatTransfer
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(air in water)
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{
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type RanzMarshall;
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residualAlpha 1e-6;
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}
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(water in air)
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{
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type RanzMarshall;
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residualAlpha 1e-6;
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}
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);
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@ -62,7 +62,6 @@ blending
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default
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{
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type linear;
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residualAlpha 1e-6;
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maxFullyDispersedAlpha.air 0.3;
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maxPartlyDispersedAlpha.air 0.5;
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maxFullyDispersedAlpha.water 0.3;
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@ -147,11 +146,13 @@ heatTransfer
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(air in water)
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{
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type RanzMarshall;
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residualAlpha 1e-6;
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}
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(water in air)
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{
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type RanzMarshall;
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residualAlpha 1e-6;
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}
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);
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@ -42,7 +42,6 @@ blending
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default
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{
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type none;
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residualAlpha 1e-3;
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continuousPhase air;
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}
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}
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@ -84,6 +83,7 @@ heatTransfer
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(particles in air)
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{
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type RanzMarshall;
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residualAlpha 1e-3;
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}
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);
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@ -41,7 +41,6 @@ blending
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default
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{
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type linear;
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residualAlpha 1e-6;
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maxFullyDispersedAlpha.air 0.3;
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maxPartlyDispersedAlpha.air 0.5;
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maxFullyDispersedAlpha.water 0.3;
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@ -126,11 +125,13 @@ heatTransfer
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(air in water)
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{
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type RanzMarshall;
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residualAlpha 1e-6;
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}
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(water in air)
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{
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type RanzMarshall;
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residualAlpha 1e-6;
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}
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);
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