155 lines
2.7 KiB
C++
155 lines
2.7 KiB
C++
/*--------------------------------*- C++ -*----------------------------------*\
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| ========= | |
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| \\ / F ield | OpenFOAM: The Open Source CFD Toolbox |
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| \\ / O peration | Version: v1912 |
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| \\ / A nd | Website: www.openfoam.com |
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| \\/ M anipulation | |
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\*---------------------------------------------------------------------------*/
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FoamFile
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{
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version 2.0;
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format ascii;
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class dictionary;
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location "constant";
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object phaseProperties;
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}
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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type thermalPhaseChangeTwoPhaseSystem;
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phases (gas liquid);
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phaseChange on;
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gas
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{
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type purePhaseModel;
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diameterModel isothermal;
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constantCoeffs
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{
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d 0.00045;
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}
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isothermalCoeffs
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{
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d0 0.00045;
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p0 1e5;
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}
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Sct 0.7;
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residualAlpha 1e-4;
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}
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liquid
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{
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type purePhaseModel;
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diameterModel constant;
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constantCoeffs
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{
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d 0.00045;
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}
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Sct 0.7;
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residualAlpha 1e-4;
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}
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blending
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{
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default
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{
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type none;
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continuousPhase liquid;
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}
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}
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surfaceTension
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();
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saturationModel
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{
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type function1;
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function csvFile;
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functionCoeffs
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{
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nHeaderLine 1;
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refColumn 0;
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componentColumns (1);
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separator ",";
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mergeSeparators no;
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file "Tsat_water_1_2bar.csv";
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outOfBounds clamp;
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interpolationScheme linear;
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};
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};
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aspectRatio
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();
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drag
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(
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(gas in liquid)
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{
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type SchillerNaumann;
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residualRe 1e-3;
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swarmCorrection
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{
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type none;
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}
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}
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);
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virtualMass
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(
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(gas in liquid)
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{
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type constantCoefficient;
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Cvm 0.5;
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}
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);
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heatTransfer.gas
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(
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(gas in liquid)
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{
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type spherical;
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residualAlpha 1e-3;
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}
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);
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heatTransfer.liquid
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(
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(gas in liquid)
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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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phaseTransfer
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();
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lift
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();
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wallLubrication
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();
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turbulentDispersion
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(
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(gas in liquid)
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{
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type Burns;
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sigma 0.7;
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Ctd 1.0;
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residualAlpha 1e-3;
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}
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);
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// Minimum allowable pressure
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pMin 10000;
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// ************************************************************************* //
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