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foam-extend4.1-coherent-io/tutorials/compressible/realFluidPisoFoam/ras/t-junction/constant/thermophysicalProperties

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/*---------------------------------------------------------------------------*\
========= |
\\ / F ield | foam-extend: Open Source CFD
\\ / O peration |
\\ / A nd | For copyright notice see file Copyright
\\/ M anipulation |
\*---------------------------------------------------------------------------*/
FoamFile
{
version 2.0;
format ascii;
class dictionary;
location "constant";
object thermophysicalProperties;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
//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 0.22394 467.6 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<redlichKwong>>>>>;
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//mixture CO2 1 44.01 73.773e5 304.13 839 1.4792e-06 116;
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//thermoType realGasHThermo<pureMixture<sutherlandTransport<realGasSpecieThermo<constantHeatCapacity<aungierRedlichKwong>>>>>;
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//thermoType realGasHThermo<pureMixture<sutherlandTransport<realGasSpecieThermo<constantHeatCapacity<pengRobinson>>>>>;
//thermoType realGasHThermo<pureMixture<sutherlandTransport<realGasSpecieThermo<constantHeatCapacity<soaveRedlichKwong>>>>>;
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//thermoType realGasHThermo<pureMixture<constRealGasTransport<realGasSpecieThermo<nasaHeatCapacityPolynomial<redlichKwong>>>>>;
//thermoType realGasHThermo<pureMixture<constRealGasTransport<realGasSpecieThermo<nasaHeatCapacityPolynomial<pengRobinson>>>>>;
//thermoType realGasHThermo<pureMixture<constRealGasTransport<realGasSpecieThermo<nasaHeatCapacityPolynomial<aungierRedlichKwong>>>>>;
//thermoType realGasHThermo<pureMixture<constRealGasTransport<realGasSpecieThermo<nasaHeatCapacityPolynomial<soaveRedlichKwong>>>>>;
//thermoType realGasHThermo<pureMixture<constRealGasTransport<realGasSpecieThermo<constantHeatCapacity<redlichKwong>>>>>;
//thermoType realGasHThermo<pureMixture<constRealGasTransport<realGasSpecieThermo<constantHeatCapacity<pengRobinson>>>>>;
//thermoType realGasHThermo<pureMixture<constRealGasTransport<realGasSpecieThermo<constantHeatCapacity<aungierRedlichKwong>>>>>;
//thermoType realGasHThermo<pureMixture<constRealGasTransport<realGasSpecieThermo<constantHeatCapacity<soaveRedlichKwong>>>>>;
//CL: description of coefficients
// *********************************************************************************************************************** //
// Coefficient:
// CO2 --> Name
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// 1
// 44.01 --> Molar Volume
// 77.773e5 --> critical pressure
// 304.13 --> critical temperatur
// 0.22394 --> acentric factor (not needed for redlich kwong)
// 467.6 --> critical density (only for aungier redlich kwong)
// 49436.5054 --> 2.849677801e-13 --> 7 heat capacity polynomial coefficent's
// .... --> two coefficent's for sutherlandRealGasTransport or for the constRealGasTransport model
// 839 --> perfect gas heat capacity Cp0 (J/kgK), needed for constantHeatCapacity
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// *********************************************************************************************************************** //