C2H6.H

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License
    This file is part of OpenFOAM.
 
    OpenFOAM is free software: you can redistribute it and/or modify it
    under the terms of the GNU General Public License as published by
    the Free Software Foundation, either version 3 of the License, or
    (at your option) any later version.
 
    OpenFOAM is distributed in the hope that it will be useful, but WITHOUT
    ANY WARRANTY; without even the implied warranty of MERCHANTABILITY or
    FITNESS FOR A PARTICULAR PURPOSE.  See the GNU General Public License
    for more details.
 
    You should have received a copy of the GNU General Public License
    along with OpenFOAM.  If not, see <http://www.gnu.org/licenses/>.
 
Class
    Foam::C2H6
 
Description
    ethane
 
SourceFiles
    C2H6.C
 
\*---------------------------------------------------------------------------*/
 
#ifndef C2H6_H
#define C2H6_H
 
#include "liquidProperties.H"
#include "NSRDS0.H"
#include "NSRDS1.H"
#include "NSRDS2.H"
#include "NSRDS3.H"
#include "NSRDS4.H"
#include "NSRDS5.H"
#include "NSRDS6.H"
#include "NSRDS7.H"
#include "NSRDS14.H"
#include "APIdiffusionCoefficient.H"
 
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
 
namespace Foam
{
 
/*---------------------------------------------------------------------------*\
                            Class C2H6 Declaration
\*---------------------------------------------------------------------------*/
 
class C2H6
:
    public liquidProperties
{
    // Private Data
 
        Function1s::NSRDS5 rho_;
        Function1s::NSRDS1 pv_;
        Function1s::NSRDS6 hl_;
        Function1s::NSRDS14 Cp_;
        Function1s::NSRDS0 h_;
        Function1s::NSRDS7 Cpg_;
        Function1s::NSRDS4 B_;
        Function1s::NSRDS1 mu_;
        Function1s::NSRDS2 mug_;
        Function1s::NSRDS0 kappa_;
        Function1s::NSRDS2 kappag_;
        Function1s::NSRDS6 sigma_;
        Function2s::APIdiffusionCoefficient D_;
 
        //- Liquid heat of formation [J/kg]
        scalar hf_;
 
 
public:
 
    friend class liquidProperties;
 
    //- Runtime type information
    TypeName("C2H6");
 
 
    // Constructors
 
        //- Construct null
        C2H6();
 
        //- Construct from components
        C2H6
        (
            const liquidProperties& l,
            const Function1s::NSRDS5& density,
            const Function1s::NSRDS1& vapourPressure,
            const Function1s::NSRDS6& heatOfVapourisation,
            const Function1s::NSRDS14& heatCapacity,
            const Function1s::NSRDS0& enthalpy,
            const Function1s::NSRDS7& idealGasHeatCapacity,
            const Function1s::NSRDS4& secondVirialCoeff,
            const Function1s::NSRDS1& dynamicViscosity,
            const Function1s::NSRDS2& vapourDynamicViscosity,
            const Function1s::NSRDS0& thermalConductivity,
            const Function1s::NSRDS2& vapourThermalConductivity,
            const Function1s::NSRDS6& surfaceTension,
            const Function2s::APIdiffusionCoefficient& vapourDiffusivity
        );
 
        //- Construct from dictionary
        C2H6(const dictionary& dict);
 
        //- Construct and return clone
        virtual autoPtr<liquidProperties> clone() const
        {
            return autoPtr<liquidProperties>(new C2H6(*this));
        }
 
 
    // Member Functions
 
        //- Liquid density [kg/m^3]
        inline scalar rho(scalar p, scalar T) const;
 
        //- Volumetric coefficient of thermal expansion [1/T]
        inline scalar alphav(scalar p, scalar T) const;
 
        //- Vapour pressure [Pa]
        inline scalar pv(scalar p, scalar T) const;
 
        //- Heat of vapourisation [J/kg]
        inline scalar hl(scalar p, scalar T) const;
 
        //- Liquid heat capacity [J/kg/K]
        inline scalar Cp(scalar p, scalar T) const;
 
        //- Liquid sensible enthalpy [J/kg]
        inline scalar hs(scalar p, scalar T) const;
 
        //- Liquid heat of formation [J/kg]
        inline scalar hf() const;
 
        //- Liquid absolute enthalpy [J/kg]
        inline scalar ha(scalar p, scalar T) const;
 
        //- Ideal gas heat capacity [J/kg/K]
        inline scalar Cpg(scalar p, scalar T) const;
 
        //- Second Virial Coefficient [m^3/kg]
        inline scalar B(scalar p, scalar T) const;
 
        //- Liquid viscosity [Pa s]
        inline scalar mu(scalar p, scalar T) const;
 
        //- Vapour viscosity [Pa s]
        inline scalar mug(scalar p, scalar T) const;
 
        //- Liquid thermal conductivity  [W/m/K]
        inline scalar kappa(scalar p, scalar T) const;
 
        //- Vapour thermal conductivity  [W/m/K]
        inline scalar kappag(scalar p, scalar T) const;
 
        //- Surface tension [N/m]
        inline scalar sigma(scalar p, scalar T) const;
 
        //- Vapour diffusivity [m^2/s]
        inline scalar D(scalar p, scalar T) const;
 
        //- Vapour diffusivity [m^2/s] with specified binary pair
        inline scalar D(scalar p, scalar T, scalar Wb) const;
 
 
    // I-O
 
        //- Write the function coefficients
        void write(Ostream& os) const;
};
 
 
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
 
} // End namespace Foam
 
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
 
#include "C2H6I.H"
 
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
 
#endif
 
// ************************************************************************* //