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  |
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FoamFile
{
    version     2.0;
    format      ascii;
    class       dictionary;

    location    "constant";
    object      thermophysicalProperties;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //

//CL: List of possible real gas models 

//thermoType  realGasHThermo<pureMixture<sutherlandTransport<realGasSpecieThermo<nasaHeatCapacityPolynomial<redlichKwong>>>>>;
//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;

//thermoType  realGasHThermo<pureMixture<sutherlandTransport<realGasSpecieThermo<nasaHeatCapacityPolynomial<aungierRedlichKwong>>>>>;
//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;

thermoType  realGasHThermo<pureMixture<sutherlandTransport<realGasSpecieThermo<nasaHeatCapacityPolynomial<pengRobinson>>>>>;
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;

//thermoType  realGasHThermo<pureMixture<sutherlandTransport<realGasSpecieThermo<nasaHeatCapacityPolynomial<soaveRedlichKwong>>>>>;
//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;

//thermoType  realGasHThermo<pureMixture<sutherlandTransport<realGasSpecieThermo<constantHeatCapacity<aungierRedlichKwong>>>>>;
//mixture CO2 1 44.01 73.773e5 304.13 467.6 0.22394  839 1.4792e-06 116;

//thermoType  realGasHThermo<pureMixture<sutherlandTransport<realGasSpecieThermo<constantHeatCapacity<pengRobinson>>>>>;
//thermoType  realGasHThermo<pureMixture<sutherlandTransport<realGasSpecieThermo<constantHeatCapacity<soaveRedlichKwong>>>>>;
//thermoType  realGasHThermo<pureMixture<constTransport<realGasSpecieThermo<nasaHeatCapacityPolynomial<redlichKwong>>>>>;
//thermoType  realGasHThermo<pureMixture<constTransport<realGasSpecieThermo<nasaHeatCapacityPolynomial<pengRobinson>>>>>;
//thermoType  realGasHThermo<pureMixture<constTransport<realGasSpecieThermo<nasaHeatCapacityPolynomial<aungierRedlichKwong>>>>>;
//thermoType  realGasHThermo<pureMixture<constTransport<realGasSpecieThermo<nasaHeatCapacityPolynomial<soaveRedlichKwong>>>>>;
//thermoType  realGasHThermo<pureMixture<constTransport<realGasSpecieThermo<constantHeatCapacity<redlichKwong>>>>>;
//thermoType  realGasHThermo<pureMixture<constTransport<realGasSpecieThermo<constantHeatCapacity<pengRobinson>>>>>;
//thermoType  realGasHThermo<pureMixture<constTransport<realGasSpecieThermo<constantHeatCapacity<aungierRedlichKwong>>>>>;
//thermoType  realGasHThermo<pureMixture<constTransport<realGasSpecieThermo<constantHeatCapacity<soaveRedlichKwong>>>>>;



//CL: description of coefficients
// *********************************************************************************************************************** //
//   Coefficient: 
//   CO2			  	--> Name
//   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 --> coefficients, see paper cited in class
//   ....				--> two coefficent's for sutherlandTransport or for the constRealGasTransport model
//   839                                --> constant cp of perfect gas (used for constantHeatCapacity)
// *********************************************************************************************************************** //