Tutorials have been updated to use the new consistent names within the wall boiling system. The changes are backwards compatible so all tutorials should run both before and after this change.
202 lines
5.1 KiB
C++
202 lines
5.1 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 | Website: https://openfoam.org
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\\ / A nd | Version: dev
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\\/ M anipulation |
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\*---------------------------------------------------------------------------*/
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FoamFile
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{
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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 populationBalanceMultiphaseSystem;
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phases (particles vapour);
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populationBalances (aggregates);
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particles
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{
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type multicomponentPhaseModel;
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diameterModel velocityGroup;
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velocityGroupCoeffs
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{
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populationBalance aggregates;
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shapeModel fractal;
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fractalCoeffs
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{
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sinteringModel KochFriedlander;
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KochFriedlanderCoeffs
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{
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Cs 8.3e24;
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n 4.0;
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m 1.0;
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Ta 3700.0;
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}
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}
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sizeGroups
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(
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f01{dSph 4.000E-10; value 1.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
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f02{dSph 5.769E-10; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
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f03{dSph 8.320E-10; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
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f04{dSph 1.200E-09; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
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f05{dSph 1.731E-09; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
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f06{dSph 2.496E-09; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
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f07{dSph 3.600E-09; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
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f08{dSph 5.192E-09; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
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f09{dSph 7.488E-09; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
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f10{dSph 1.080E-08; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
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f11{dSph 1.558E-08; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
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f12{dSph 2.246E-08; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
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f13{dSph 3.240E-08; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
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f14{dSph 4.673E-08; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
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f15{dSph 6.739E-08; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
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f16{dSph 9.720E-08; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
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f17{dSph 1.402E-07; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
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f18{dSph 2.022E-07; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
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f19{dSph 2.916E-07; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
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f20{dSph 4.206E-07; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
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f21{dSph 6.066E-07; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
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f22{dSph 8.748E-07; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
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f23{dSph 1.262E-06; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
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f24{dSph 1.820E-06; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
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f25{dSph 2.624E-06; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
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f26{dSph 3.785E-06; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
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f27{dSph 5.459E-06; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
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f28{dSph 7.873E-06; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
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f29{dSph 1.136E-05; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
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);
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}
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residualAlpha 1e-15;
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}
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vapour
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{
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type reactingPhaseModel;
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diameterModel none;
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residualAlpha 1e-5;
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}
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populationBalanceCoeffs
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{
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aggregates
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{
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continuousPhase vapour;
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coalescenceModels
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(
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DahnekeInterpolation
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{
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sigma 340e-12;
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}
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);
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binaryBreakupModels
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();
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breakupModels
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();
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driftModels
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();
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nucleationModels
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(
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reactionDriven
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{
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nucleationDiameter 4E-10;
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velocityGroup particles;
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reactingPhase vapour;
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dmdtf phaseTransfer:dmidtf;
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specie TiO2;
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}
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);
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}
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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 continuous;
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phase vapour;
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}
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}
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interfaceCompression
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{}
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surfaceTension
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{}
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drag
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{
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particles_dispersedIn_vapour
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{
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type timeScaleFiltered;
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minRelaxTime 1e-4;
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dragModel
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{
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type aerosolDrag;
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sigma 340e-12;
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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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heatTransfer
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{
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particles_dispersedIn_vapour
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{
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type timeScaleFiltered;
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minRelaxTime 1e-4;
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heatTransferModel
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{
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type constantNu;
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Nu 1;
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}
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}
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}
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phaseTransfer
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{
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particles_dispersedIn_vapour
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{
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type reactionDriven;
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reactingPhase vapour;
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targetPhase particles;
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species (TiO2);
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}
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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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interfaceCompression
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{}
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// ************************************************************************* //
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