compressible::alphatWallBoilingWallFunction: Naming consistency
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.
This commit is contained in:
@ -33,7 +33,7 @@ boundaryField
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{
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type compressible::alphatWallBoilingWallFunction;
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otherPhase liquid;
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phaseType vapor;
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phaseType vapour;
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Prt 0.85;
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partitioningModel
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{
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@ -47,14 +47,14 @@ boundaryField
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NRef 30000000;
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deltaTRef 10;
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}
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departureDiamModel
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departureDiameterModel
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{
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type TolubinskiKostanchuk;
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dRef 0.00024;
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dMax 0.0014;
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dMin 1e-06;
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}
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departureFreqModel
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departureFrequencyModel
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{
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type KocamustafaogullariIshii;
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Cf 1.18;
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@ -50,7 +50,7 @@ gnuplot<<EOF
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'./postProcessing/fluid/outflow/$surfaceFile' \
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every ::10::20000 u 1:(360*\$3) w l lt 3 t 'liquid outflow', \
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'./postProcessing/fluid/outflow/$surfaceFile' \
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every ::10::20000 u 1:(360*\$2+360*\$3) w l lt 4 t 'liquid + vapor outflow'
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every ::10::20000 u 1:(360*\$2+360*\$3) w l lt 4 t 'liquid + vapour outflow'
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set ylabel 'Enthalpy in- and outflow (J/s)'
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set yrange [1.5e5:2.0e5]
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@ -64,7 +64,7 @@ gnuplot<<EOF
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"<paste \
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./postProcessing/fluid/outletLiquid/$surfaceFile \
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./postProcessing/fluid/outletGas/$surfaceFile" \
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every ::10::20000 u 1:(360*\$2+360*\$4) w l lt 4 t 'liquid + vapor outflow'
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every ::10::20000 u 1:(360*\$2+360*\$4) w l lt 4 t 'liquid + vapour outflow'
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unset multiplot
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@ -9,7 +9,7 @@ FoamFile
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{
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format ascii;
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class volScalarField;
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object Ar.vapor;
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object Ar.vapour;
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}
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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@ -9,7 +9,7 @@ FoamFile
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{
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format ascii;
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class volScalarField;
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object TiO2.vapor;
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object Cl2.vapour;
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}
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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@ -9,7 +9,7 @@ FoamFile
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{
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format ascii;
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class volScalarField;
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object Cl2.vapor;
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object N2.vapour;
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}
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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@ -9,7 +9,7 @@ FoamFile
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{
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format ascii;
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class volScalarField;
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object O2.vapor;
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object O2.vapour;
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}
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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@ -9,7 +9,7 @@ FoamFile
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{
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format ascii;
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class volScalarField;
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object T.vapor;
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object T.vapour;
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}
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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@ -9,7 +9,7 @@ FoamFile
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{
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format ascii;
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class volScalarField;
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object TiCl4.vapor;
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object TiCl4.vapour;
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}
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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@ -9,7 +9,7 @@ FoamFile
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{
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format ascii;
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class volScalarField;
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object N2.vapor;
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object TiO2.vapour;
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}
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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@ -9,7 +9,7 @@ FoamFile
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{
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format ascii;
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class volVectorField;
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object U.vapor;
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object U.vapour;
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}
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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@ -25,7 +25,7 @@ boundaryField
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{
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type flowRateInletVelocity;
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massFlowRate 2.173893e-07;
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rho rho.vapor;
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rho rho.vapour;
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profile laminarBL;
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value $internalField;
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}
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@ -30,9 +30,9 @@ boundaryField
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outlet
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{
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type prghTotalPressure;
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U U.vapor;
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phi phi.vapor;
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rho rho.vapor;
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U U.vapour;
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phi phi.vapour;
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rho rho.vapour;
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p0 uniform 1e5;
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value $internalField;
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}
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@ -35,6 +35,6 @@ odeCoeffs
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relTol 0.01;
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}
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#include "reactions.vapor"
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#include "reactions.vapour"
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// ************************************************************************* //
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@ -10,7 +10,7 @@ FoamFile
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format ascii;
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class dictionary;
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location "constant";
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object combustionProperties.vapor;
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object combustionProperties.vapour;
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}
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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@ -10,7 +10,7 @@ FoamFile
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format ascii;
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class dictionary;
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location "constant";
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object momentumTransport.vapor;
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object momentumTransport.vapour;
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}
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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@ -16,7 +16,7 @@ FoamFile
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type populationBalanceMultiphaseSystem;
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phases (particles vapor);
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phases (particles vapour);
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populationBalances (aggregates);
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@ -82,7 +82,7 @@ particles
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residualAlpha 1e-15;
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}
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vapor
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vapour
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{
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type reactingPhaseModel;
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@ -95,7 +95,7 @@ populationBalanceCoeffs
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{
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aggregates
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{
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continuousPhase vapor;
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continuousPhase vapour;
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coalescenceModels
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(
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@ -120,7 +120,7 @@ populationBalanceCoeffs
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{
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nucleationDiameter 4E-10;
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velocityGroup particles;
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reactingPhase vapor;
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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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@ -133,7 +133,7 @@ blending
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default
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{
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type continuous;
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phase vapor;
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phase vapour;
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}
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}
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@ -145,7 +145,7 @@ surfaceTension
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drag
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{
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particles_dispersedIn_vapor
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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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@ -162,7 +162,7 @@ virtualMass
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heatTransfer
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{
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particles_dispersedIn_vapor
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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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@ -177,10 +177,10 @@ heatTransfer
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phaseTransfer
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{
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particles_dispersedIn_vapor
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particles_dispersedIn_vapour
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{
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type reactionDriven;
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reactingPhase vapor;
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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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@ -10,7 +10,7 @@ FoamFile
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format ascii;
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class dictionary;
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location "constant";
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object physicalProperties.vapor;
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object physicalProperties.vapour;
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}
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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@ -27,7 +27,7 @@ thermoType
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defaultSpecie Ar;
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#include "$FOAM_CASE/constant/thermo.vapor"
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#include "$FOAM_CASE/constant/thermo.vapour"
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// ************************************************************************* //
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@ -16,7 +16,7 @@ FoamFile
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format ascii;
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class dictionary;
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location "constant";
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object reactions.vapor;
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object reactions.vapour;
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}
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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@ -10,7 +10,7 @@ FoamFile
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format ascii;
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class dictionary;
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location "constant";
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object thermo.vapor;
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object thermo.vapour;
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}
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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@ -59,7 +59,7 @@ functions
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funcName=graph,
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start=(0 0 1e-3),
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end=(0.44 0 1e-3),
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fields=(TiCl4.vapor O2.vapor Cl2.vapor alpha.particles)
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fields=(TiCl4.vapour O2.vapour Cl2.vapour alpha.particles)
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)
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#includeFunc populationBalanceSizeDistribution
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@ -9,7 +9,7 @@ FoamFile
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{
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format ascii;
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class volScalarField;
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object Ar.vapor;
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object Ar.vapour;
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}
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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@ -9,7 +9,7 @@ FoamFile
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{
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format ascii;
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class volScalarField;
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object O2.vapor;
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object O2.vapour;
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}
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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@ -9,7 +9,7 @@ FoamFile
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{
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format ascii;
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class volScalarField;
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object T.vapor;
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object T.vapour;
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}
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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@ -9,7 +9,7 @@ FoamFile
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{
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format ascii;
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class volScalarField;
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object TiCl4.vapor;
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object TiCl4.vapour;
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}
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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@ -9,7 +9,7 @@ FoamFile
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{
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format ascii;
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class volVectorField;
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object U.vapor;
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object U.vapour;
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}
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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@ -25,7 +25,7 @@ boundaryField
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{
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type flowRateInletVelocity;
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massFlowRate 2.173893e-07;
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rho rho.vapor;
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rho rho.vapour;
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profile laminarBL;
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value $internalField;
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}
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@ -9,7 +9,7 @@ FoamFile
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{
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format ascii;
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class volScalarField;
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object Ydefault.vapor;
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object Ydefault.vapour;
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}
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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@ -30,9 +30,9 @@ boundaryField
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outlet
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{
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type prghTotalPressure;
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U U.vapor;
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phi phi.vapor;
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rho rho.vapor;
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U U.vapour;
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phi phi.vapour;
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rho rho.vapour;
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p0 uniform 1e5;
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value $internalField;
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}
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@ -35,6 +35,6 @@ odeCoeffs
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relTol 0.01;
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}
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#include "reactions.vapor"
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#include "reactions.vapour"
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// ************************************************************************* //
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@ -10,7 +10,7 @@ FoamFile
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format ascii;
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class dictionary;
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location "constant";
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object combustionProperties.vapor;
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object combustionProperties.vapour;
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}
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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@ -10,7 +10,7 @@ FoamFile
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format ascii;
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class dictionary;
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location "constant";
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object momentumTransport.vapor;
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object momentumTransport.vapour;
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}
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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@ -16,7 +16,7 @@ FoamFile
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type populationBalanceMultiphaseSystem;
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phases (particles vapor);
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phases (particles vapour);
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populationBalances (aggregates);
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@ -84,7 +84,7 @@ particles
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residualAlpha 1e-15;
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}
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vapor
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vapour
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{
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type reactingPhaseModel;
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@ -99,7 +99,7 @@ populationBalanceCoeffs
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{
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aggregates
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{
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continuousPhase vapor;
|
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continuousPhase vapour;
|
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coalescenceModels
|
||||
(
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@ -119,7 +119,7 @@ populationBalanceCoeffs
|
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(
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phaseChange
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{
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interfaces (particles_vapor);
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interfaces (particles_vapour);
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dmdtf phaseTransfer:dmidtf;
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specie TiO2_s;
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surfaceGrowthType ParkRogak;
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@ -132,7 +132,7 @@ populationBalanceCoeffs
|
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{
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nucleationDiameter 4E-10;
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velocityGroup particles;
|
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reactingPhase vapor;
|
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reactingPhase vapour;
|
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dmdtf phaseTransfer:dmidtf;
|
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specie TiO2;
|
||||
}
|
||||
@ -145,7 +145,7 @@ blending
|
||||
default
|
||||
{
|
||||
type continuous;
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phase vapor;
|
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phase vapour;
|
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}
|
||||
}
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||||
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@ -157,7 +157,7 @@ surfaceTension
|
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drag
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||||
{
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||||
particles_dispersedIn_vapor
|
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particles_dispersedIn_vapour
|
||||
{
|
||||
type timeScaleFiltered;
|
||||
minRelaxTime 1e-4;
|
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@ -174,7 +174,7 @@ virtualMass
|
||||
|
||||
heatTransfer
|
||||
{
|
||||
particles_dispersedIn_vapor
|
||||
particles_dispersedIn_vapour
|
||||
{
|
||||
type timeScaleFiltered;
|
||||
minRelaxTime 1e-4;
|
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@ -189,10 +189,10 @@ heatTransfer
|
||||
|
||||
phaseTransfer
|
||||
{
|
||||
particles_dispersedIn_vapor
|
||||
particles_dispersedIn_vapour
|
||||
{
|
||||
type reactionDriven;
|
||||
reactingPhase vapor;
|
||||
reactingPhase vapour;
|
||||
targetPhase particles;
|
||||
species (TiO2 TiO2_s);
|
||||
}
|
||||
|
||||
@ -10,7 +10,7 @@ FoamFile
|
||||
format ascii;
|
||||
class dictionary;
|
||||
location "constant";
|
||||
object physicalProperties.vapor;
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||||
object physicalProperties.vapour;
|
||||
}
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||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
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@ -27,7 +27,7 @@ thermoType
|
||||
|
||||
defaultSpecie Ar;
|
||||
|
||||
#include "$FOAM_CASE/constant/thermo.vapor"
|
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#include "$FOAM_CASE/constant/thermo.vapour"
|
||||
|
||||
|
||||
// ************************************************************************* //
|
||||
@ -20,7 +20,7 @@ FoamFile
|
||||
format ascii;
|
||||
class dictionary;
|
||||
location "constant";
|
||||
object reactions.vapor;
|
||||
object reactions.vapour;
|
||||
}
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
@ -10,7 +10,7 @@ FoamFile
|
||||
format ascii;
|
||||
class dictionary;
|
||||
location "constant";
|
||||
object thermo.vapor;
|
||||
object thermo.vapour;
|
||||
}
|
||||
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
|
||||
|
||||
@ -59,7 +59,7 @@ functions
|
||||
funcName=graph,
|
||||
start=(0 0 1e-3),
|
||||
end=(0.44 0 1e-3),
|
||||
fields=(TiCl4.vapor O2.vapor Cl2.vapor alpha.particles)
|
||||
fields=(TiCl4.vapour O2.vapour Cl2.vapour alpha.particles)
|
||||
)
|
||||
|
||||
#includeFunc populationBalanceSizeDistribution
|
||||
|
||||
@ -34,7 +34,7 @@ boundaryField
|
||||
{
|
||||
type compressible::alphatWallBoilingWallFunction;
|
||||
otherPhase liquid;
|
||||
phaseType vapor;
|
||||
phaseType vapour;
|
||||
Prt 0.85;
|
||||
partitioningModel
|
||||
{
|
||||
|
||||
@ -48,14 +48,14 @@ boundaryField
|
||||
NRef 30000000;
|
||||
deltaTRef 10;
|
||||
}
|
||||
departureDiamModel
|
||||
departureDiameterModel
|
||||
{
|
||||
type TolubinskiKostanchuk;
|
||||
dRef 0.00024;
|
||||
dMax 0.0014;
|
||||
dMin 1e-06;
|
||||
}
|
||||
departureFreqModel
|
||||
departureFrequencyModel
|
||||
{
|
||||
type KocamustafaogullariIshii;
|
||||
Cf 1.18;
|
||||
|
||||
@ -57,7 +57,7 @@ gnuplot<<EOF
|
||||
'./postProcessing/outflow/$surfaceFile' \
|
||||
every ::4::10000 u 1:(360*\$3) w l lt 3 t 'liquid outflow', \
|
||||
'./postProcessing/outflow/$surfaceFile' \
|
||||
every ::4::10000 u 1:(360*\$2+360*\$3) w l lt 4 t 'liquid + vapor outflow'
|
||||
every ::4::10000 u 1:(360*\$2+360*\$3) w l lt 4 t 'liquid + vapour outflow'
|
||||
|
||||
set ylabel 'Enthalpy in- and outflow (J/s)'
|
||||
set yrange [1.5e5:2.0e5]
|
||||
@ -71,7 +71,7 @@ gnuplot<<EOF
|
||||
"<paste \
|
||||
./postProcessing/outletLiquid/$surfaceFile \
|
||||
./postProcessing/outletGas/$surfaceFile" \
|
||||
every ::4::10000 u 1:(360*\$2+360*\$4) w l lt 4 t 'liquid + vapor outflow'
|
||||
every ::4::10000 u 1:(360*\$2+360*\$4) w l lt 4 t 'liquid + vapour outflow'
|
||||
|
||||
unset multiplot
|
||||
|
||||
|
||||
@ -34,7 +34,7 @@ boundaryField
|
||||
{
|
||||
type compressible::alphatWallBoilingWallFunction;
|
||||
otherPhase liquid;
|
||||
phaseType vapor;
|
||||
phaseType vapour;
|
||||
Prt 0.85;
|
||||
partitioningModel
|
||||
{
|
||||
|
||||
@ -48,14 +48,14 @@ boundaryField
|
||||
NRef 30000000;
|
||||
deltaTRef 10;
|
||||
}
|
||||
departureDiamModel
|
||||
departureDiameterModel
|
||||
{
|
||||
type TolubinskiKostanchuk;
|
||||
dRef 0.00024;
|
||||
dMax 0.0014;
|
||||
dMin 1e-06;
|
||||
}
|
||||
departureFreqModel
|
||||
departureFrequencyModel
|
||||
{
|
||||
type KocamustafaogullariIshii;
|
||||
Cf 1.18;
|
||||
|
||||
@ -57,7 +57,7 @@ gnuplot<<EOF
|
||||
'./postProcessing/outflow/$surfaceFile' \
|
||||
every ::4::10000 u 1:(360*\$3) w l lt 3 t 'liquid outflow', \
|
||||
'./postProcessing/outflow/$surfaceFile' \
|
||||
every ::4::10000 u 1:(360*\$2+360*\$3) w l lt 4 t 'liquid + vapor outflow'
|
||||
every ::4::10000 u 1:(360*\$2+360*\$3) w l lt 4 t 'liquid + vapour outflow'
|
||||
|
||||
set ylabel 'Enthalpy in- and outflow (J/s)'
|
||||
set yrange [1.5e5:2.0e5]
|
||||
@ -71,7 +71,7 @@ gnuplot<<EOF
|
||||
"<paste \
|
||||
./postProcessing/outletLiquid/$surfaceFile \
|
||||
./postProcessing/outletGas/$surfaceFile" \
|
||||
every ::4::10000 u 1:(360*\$2+360*\$4) w l lt 4 t 'liquid + vapor outflow'
|
||||
every ::4::10000 u 1:(360*\$2+360*\$4) w l lt 4 t 'liquid + vapour outflow'
|
||||
|
||||
unset multiplot
|
||||
|
||||
|
||||
@ -34,7 +34,7 @@ boundaryField
|
||||
{
|
||||
type compressible::alphatWallBoilingWallFunction;
|
||||
otherPhase liquid;
|
||||
phaseType vapor;
|
||||
phaseType vapour;
|
||||
Prt 0.85;
|
||||
partitioningModel
|
||||
{
|
||||
|
||||
@ -34,7 +34,7 @@ boundaryField
|
||||
{
|
||||
type compressible::alphatWallBoilingWallFunction;
|
||||
otherPhase liquid;
|
||||
phaseType vapor;
|
||||
phaseType vapour;
|
||||
Prt 0.85;
|
||||
partitioningModel
|
||||
{
|
||||
|
||||
@ -48,14 +48,14 @@ boundaryField
|
||||
NRef 30000000;
|
||||
deltaTRef 10;
|
||||
}
|
||||
departureDiamModel
|
||||
departureDiameterModel
|
||||
{
|
||||
type TolubinskiKostanchuk;
|
||||
dRef 0.00024;
|
||||
dMax 0.0014;
|
||||
dMin 1e-06;
|
||||
}
|
||||
departureFreqModel
|
||||
departureFrequencyModel
|
||||
{
|
||||
type KocamustafaogullariIshii;
|
||||
Cf 1.18;
|
||||
|
||||
@ -57,7 +57,7 @@ gnuplot<<EOF
|
||||
'./postProcessing/outflow/$surfaceFile' \
|
||||
every ::4::10000 u 1:(360*\$4) w l lt 3 t 'liquid outflow', \
|
||||
'./postProcessing/outflow/$surfaceFile' \
|
||||
every ::4::10000 u 1:(360*\$2+360*\$3+360*\$4) w l lt 4 t 'liquid + vapor outflow'
|
||||
every ::4::10000 u 1:(360*\$2+360*\$3+360*\$4) w l lt 4 t 'liquid + vapour outflow'
|
||||
|
||||
set ylabel 'Enthalpy in- and outflow (J/s)'
|
||||
set yrange [1.5e5:2.0e5]
|
||||
@ -72,7 +72,7 @@ gnuplot<<EOF
|
||||
./postProcessing/outletLiquid/$surfaceFile \
|
||||
./postProcessing/outletGas/$surfaceFile \
|
||||
./postProcessing/outletGas2/$surfaceFile" \
|
||||
every ::4::10000 u 1:(360*\$2+360*\$4+360*\$6) w l lt 4 t 'liquid + vapor outflow'
|
||||
every ::4::10000 u 1:(360*\$2+360*\$4+360*\$6) w l lt 4 t 'liquid + vapour outflow'
|
||||
|
||||
unset multiplot
|
||||
|
||||
|
||||
Reference in New Issue
Block a user