ee238cd77e
Conflicts: src/thermophysicalModels/specie/thermo/realGasThermo/constantHeatCapacity/constantHeatCapacity.C src/thermophysicalModels/specie/thermo/realGasThermo/constantHeatCapacity/constantHeatCapacityI.H src/thermophysicalModels/specie/transport/constRealGas/constRealGasTransport.C src/thermophysicalModels/specie/transport/constRealGas/constRealGasTransport.H src/thermophysicalModels/specie/transport/constRealGas/constRealGasTransportI.H tutorials/compressible/realFluidPisoFoam/ras/backStep/constant/thermophysicalProperties tutorials/compressible/realFluidPisoFoam/ras/cavity_IAPWS97/0.org/omega tutorials/compressible/realFluidPisoFoam/ras/cavity_IAPWS97/0/omega tutorials/compressible/realFluidPisoFoam/ras/t-junction/constant/thermophysicalProperties
63 lines
4.2 KiB
Text
Executable file
63 lines
4.2 KiB
Text
Executable file
/*---------------------------------------------------------------------------*\
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========= |
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\\ / F ield | foam-extend: Open Source CFD
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\\ / O peration | Version: 4.0
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\\ / A nd | Web: http://www.foam-extend.org
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\\/ M anipulation | For copyright notice see file Copyright
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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 thermophysicalProperties;
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}
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// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
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//CL: List of possible real gas models
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//thermoType realGasHThermo<pureMixture<sutherlandTransport<realGasSpecieThermo<nasaHeatCapacityPolynomial<redlichKwong>>>>>;
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//mixture CO2 1 44.01 73.773e5 304.13 49436.5054 -626.411601 5.30172524 0.002503813816 -0.0000002127308728 -0.000000000768998878 2.849677801e-13 1.4792e-06 116;
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//thermoType realGasHThermo<pureMixture<sutherlandTransport<realGasSpecieThermo<nasaHeatCapacityPolynomial<aungierRedlichKwong>>>>>;
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//mixture CO2 1 44.01 73.773e5 304.13 467.6 0.22394 49436.5054 -626.411601 5.30172524 0.002503813816 -0.0000002127308728 -0.000000000768998878 2.849677801E-13 1.4792e-06 116;
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thermoType realGasHThermo<pureMixture<sutherlandTransport<realGasSpecieThermo<nasaHeatCapacityPolynomial<pengRobinson>>>>>;
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mixture CO2 1 44.01 73.773e5 304.13 0.22394 49436.5054 -626.411601 5.30172524 0.002503813816 -0.0000002127308728 -0.000000000768998878 2.849677801e-13 1.4792e-06 116;
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//thermoType realGasHThermo<pureMixture<sutherlandTransport<realGasSpecieThermo<nasaHeatCapacityPolynomial<soaveRedlichKwong>>>>>;
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//mixture CO2 1 44.01 73.773e5 304.13 0.22394 49436.5054 -626.411601 5.30172524 0.002503813816 -0.0000002127308728 -0.000000000768998878 2.849677801e-13 1.4792e-06 116;
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//thermoType realGasHThermo<pureMixture<sutherlandTransport<realGasSpecieThermo<constantHeatCapacity<aungierRedlichKwong>>>>>;
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//mixture CO2 1 44.01 73.773e5 304.13 467.6 0.22394 839 1.4792e-06 116;
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//thermoType realGasHThermo<pureMixture<sutherlandTransport<realGasSpecieThermo<constantHeatCapacity<pengRobinson>>>>>;
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//thermoType realGasHThermo<pureMixture<sutherlandTransport<realGasSpecieThermo<constantHeatCapacity<soaveRedlichKwong>>>>>;
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//thermoType realGasHThermo<pureMixture<constTransport<realGasSpecieThermo<nasaHeatCapacityPolynomial<redlichKwong>>>>>;
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//thermoType realGasHThermo<pureMixture<constTransport<realGasSpecieThermo<nasaHeatCapacityPolynomial<pengRobinson>>>>>;
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//thermoType realGasHThermo<pureMixture<constTransport<realGasSpecieThermo<nasaHeatCapacityPolynomial<aungierRedlichKwong>>>>>;
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//thermoType realGasHThermo<pureMixture<constTransport<realGasSpecieThermo<nasaHeatCapacityPolynomial<soaveRedlichKwong>>>>>;
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//thermoType realGasHThermo<pureMixture<constTransport<realGasSpecieThermo<constantHeatCapacity<redlichKwong>>>>>;
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//thermoType realGasHThermo<pureMixture<constTransport<realGasSpecieThermo<constantHeatCapacity<pengRobinson>>>>>;
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//thermoType realGasHThermo<pureMixture<constTransport<realGasSpecieThermo<constantHeatCapacity<aungierRedlichKwong>>>>>;
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//thermoType realGasHThermo<pureMixture<constTransport<realGasSpecieThermo<constantHeatCapacity<soaveRedlichKwong>>>>>;
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//CL: description of coefficients
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// *********************************************************************************************************************** //
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// Coefficient:
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// CO2 --> Name
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// 1
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// 44.01 --> Molar Volume
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// 77.773e5 --> critical pressure
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// 304.13 --> critical temperatur
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// 0.22394 --> acentric factor (not needed for redlich kwong)
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// 467.6 --> critical density (only for aungier redlich kwong)
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// 49436.5054 --> 2.849677801e-13 --> 7 heat capacity polynomial coefficents --> coefficients, see paper cited in class
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// .... --> two coefficents for sutherlandRealGasTransport or for the constRealGasTransport model
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// 839 --> constant cp of perfect gas (used for constantHeatCapacity)
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// *********************************************************************************************************************** //
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