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INT: Org integration of VOF, Euler phase solvers and models.
Integration of VOF MULES new interfaces. Update of VOF solvers and all instances of MULES in the code. Integration of reactingTwoPhaseEuler and reactingMultiphaseEuler solvers and sub-models Updating reactingEuler tutorials accordingly (most of them tested) New eRefConst thermo used in tutorials. Some modifications at thermo specie level affecting mostly eThermo. hThermo mostly unaffected New chtMultiRegionTwoPhaseEulerFoam solver for quenching and tutorial. Phases sub-models for reactingTwoPhaseEuler and reactingMultiphaseEuler were moved to src/phaseSystemModels/reactingEulerFoam in order to be used by BC for chtMultiRegionTwoPhaseEulerFoam. Update of interCondensatingEvaporatingFoam solver.
This commit is contained in:
Sergio Ferraris
committed by
Andrew Heather
Andrew Heather
parent
0628bfb017
commit
8170f2ad92
@ -15,7 +15,7 @@ FoamFile
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}
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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type heatAndMomentumTransferMultiphaseSystem;
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type basicMultiphaseSystem;
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phases (air water);
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@ -47,6 +47,14 @@ water
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blending
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{
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default
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{
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type linear;
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minFullyContinuousAlpha.air 0.7;
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minPartlyContinuousAlpha.air 0.3;
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minFullyContinuousAlpha.water 0.7;
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minPartlyContinuousAlpha.water 0.3;
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}
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drag
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{
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type linear;
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minFullyContinuousAlpha.air 0.7;
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@ -150,6 +158,9 @@ heatTransfer
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}
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);
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phaseTransfer
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();
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lift
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();
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@ -20,7 +20,7 @@ thermoType
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type heRhoThermo;
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mixture pureMixture;
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transport const;
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thermo hConst;
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thermo eConst;
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equationOfState perfectFluid;
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specie specie;
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energy sensibleInternalEnergy;
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@ -39,7 +39,7 @@ mixture
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}
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thermodynamics
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{
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Cp 4195;
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Cv 4195;
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Hf 0;
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}
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transport
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@ -29,7 +29,7 @@ deltaT 0.005;
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writeControl runTime;
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writeInterval 1;
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writeInterval 10;
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purgeWrite 0;
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@ -51,7 +51,7 @@ maxCo 0.5;
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maxDeltaT 1;
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functions0
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functions
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{
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fieldAverage1
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{
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@ -18,6 +18,7 @@ FoamFile
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defaultFieldValues
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(
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volScalarFieldValue alpha.air 1
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volScalarFieldValue alpha.water 0
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);
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regions
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@ -28,6 +29,7 @@ regions
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fieldValues
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(
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volScalarFieldValue alpha.air 0
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volScalarFieldValue alpha.water 1
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);
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}
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);
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@ -15,7 +15,7 @@ FoamFile
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}
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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type heatAndMomentumTransferMultiphaseSystem;
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type basicMultiphaseSystem;
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phases (water oil mercury air);
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@ -82,6 +82,19 @@ blending
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minFullyContinuousAlpha.air 0.7;
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minPartlyContinuousAlpha.air 0.5;
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}
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/*
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drag
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{
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type linear;
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minFullyContinuousAlpha.water 0.7;
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minPartlyContinuousAlpha.water 0.3;
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minFullyContinuousAlpha.oil 0.7;
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minPartlyContinuousAlpha.oil 0.3;
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minFullyContinuousAlpha.mercury 0.7;
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minPartlyContinuousAlpha.mercury 0.3;
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minFullyContinuousAlpha.air 0.7;
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minPartlyContinuousAlpha.air 0.3;
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}*/
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}
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surfaceTension
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@ -446,6 +459,9 @@ heatTransfer
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lift
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();
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phaseTransfer
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();
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wallLubrication
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();
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@ -26,6 +26,8 @@ thermoType
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energy sensibleInternalEnergy;
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}
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pressureWorkAlphaLimit 0.99;
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mixture
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{
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specie
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@ -20,7 +20,7 @@ thermoType
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type heRhoThermo;
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mixture pureMixture;
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transport const;
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thermo hConst;
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thermo eConst;
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equationOfState rhoConst;
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specie specie;
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energy sensibleInternalEnergy;
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@ -38,7 +38,7 @@ mixture
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}
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thermodynamics
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{
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Cp 135;
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Cv 135;
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Hf 0;
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}
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transport
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@ -20,7 +20,7 @@ thermoType
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type heRhoThermo;
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mixture pureMixture;
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transport const;
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thermo hConst;
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thermo eConst;
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equationOfState rhoConst;
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specie specie;
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energy sensibleInternalEnergy;
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@ -38,7 +38,7 @@ mixture
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}
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thermodynamics
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{
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Cp 4195;
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Cv 4195;
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Hf 0;
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}
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transport
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@ -20,7 +20,7 @@ thermoType
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type heRhoThermo;
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mixture pureMixture;
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transport const;
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thermo hConst;
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thermo eConst;
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equationOfState perfectFluid;
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specie specie;
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energy sensibleInternalEnergy;
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@ -39,7 +39,7 @@ mixture
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}
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thermodynamics
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{
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Cp 4195;
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Cv 4195;
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Hf 0;
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}
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transport
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@ -17,9 +17,9 @@ FoamFile
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application reactingMultiphaseEulerFoam;
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startFrom startTime;
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startFrom latestTime;
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startTime 0;
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startTime 0.6;
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stopAt endTime;
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@ -47,7 +47,7 @@ runTimeModifiable yes;
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adjustTimeStep yes;
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maxCo 0.5;
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maxCo 0.2;
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maxDeltaT 1;
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@ -30,8 +30,8 @@ divSchemes
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"div\(phi,alpha.*\)" Gauss vanLeer;
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"div\(phir,alpha.*,alpha.*\)" Gauss vanLeer;
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"div\(alphaRhoPhi.*,U.*\)" Gauss limitedLinearV 1;
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"div\(phi.*,U.*\)" Gauss limitedLinearV 1;
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"div\(alphaRhoPhi.*,U.*\)" Gauss limitedLinear 1;
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"div\(phi.*,U.*\)" Gauss limitedLinear 1;
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"div\(alphaRhoPhi.*,(h|e).*\)" Gauss limitedLinear 1;
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"div\(alphaRhoPhi.*,K.*\)" Gauss limitedLinear 1;
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@ -19,7 +19,8 @@ solvers
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{
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"alpha.*"
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{
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nAlphaSubCycles 2;
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nAlphaCorr 1;
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nAlphaSubCycles 2;
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}
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p_rgh
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@ -32,6 +33,7 @@ solvers
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p_rghFinal
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{
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$p_rgh;
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solver PCG;
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preconditioner
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{
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@ -76,8 +78,9 @@ solvers
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PIMPLE
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{
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nOuterCorrectors 1;
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nCorrectors 3;
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nCorrectors 3;
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nNonOrthogonalCorrectors 0;
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faceMomentum false;
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pRefCell 0;
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pRefValue 0;
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