Files
openfoam/src/thermophysicalModels/liquidProperties/C2H6/C2H6.H
andy 497b4f0bed ENH: Code refactoring to avoing ambiguities + clean-up
- pointSolid->solidProperties
- pointSolidMixure->solidMixtureProperties
- liquids->liquidProperties
- liquidMixture->liquidMoxtureProperties
2011-01-28 13:09:10 +00:00

213 lines
5.9 KiB
C++

/*---------------------------------------------------------------------------*\
========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration |
\\ / A nd | Copyright (C) 2004-2011 OpenCFD Ltd.
\\/ M anipulation |
-------------------------------------------------------------------------------
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 "NSRDSfunc0.H"
#include "NSRDSfunc1.H"
#include "NSRDSfunc2.H"
#include "NSRDSfunc3.H"
#include "NSRDSfunc4.H"
#include "NSRDSfunc5.H"
#include "NSRDSfunc6.H"
#include "NSRDSfunc7.H"
#include "NSRDSfunc14.H"
#include "APIdiffCoefFunc.H"
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
namespace Foam
{
/*---------------------------------------------------------------------------*\
Class C2H6 Declaration
\*---------------------------------------------------------------------------*/
class C2H6
:
public liquidProperties
{
// Private data
NSRDSfunc5 rho_;
NSRDSfunc1 pv_;
NSRDSfunc6 hl_;
NSRDSfunc14 Cp_;
NSRDSfunc0 h_;
NSRDSfunc7 Cpg_;
NSRDSfunc4 B_;
NSRDSfunc1 mu_;
NSRDSfunc2 mug_;
NSRDSfunc0 K_;
NSRDSfunc2 Kg_;
NSRDSfunc6 sigma_;
APIdiffCoefFunc D_;
public:
//- Runtime type information
TypeName("C2H6");
// Constructors
//- Construct null
C2H6();
//- Construct from components
C2H6
(
const liquidProperties& l,
const NSRDSfunc5& density,
const NSRDSfunc1& vapourPressure,
const NSRDSfunc6& heatOfVapourisation,
const NSRDSfunc14& heatCapacity,
const NSRDSfunc0& enthalpy,
const NSRDSfunc7& idealGasHeatCapacity,
const NSRDSfunc4& secondVirialCoeff,
const NSRDSfunc1& dynamicViscosity,
const NSRDSfunc2& vapourDynamicViscosity,
const NSRDSfunc0& thermalConductivity,
const NSRDSfunc2& vapourThermalConductivity,
const NSRDSfunc6& surfaceTension,
const APIdiffCoefFunc& vapourDiffussivity
);
//- Construct from Istream
C2H6(Istream& is);
//- Construct from dictionary
C2H6(const dictionary& dict);
//- Construct copy
C2H6(const C2H6& liq);
//- 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;
//- 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 Enthalpy [J/(kg)]
inline scalar h(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 K(scalar p, scalar T) const;
//- Vapour thermal conductivity [W/(m K)]
inline scalar Kg(scalar p, scalar T) const;
//- Surface tension [N/m]
inline scalar sigma(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s]
inline scalar D(scalar p, scalar T) const;
//- Vapour diffussivity [m2/s] with specified binary pair
inline scalar D(scalar p, scalar T, scalar Wb) const;
// I-O
//- Write the function coefficients
void writeData(Ostream& os) const
{
liquidProperties::writeData(os); os << nl;
rho_.writeData(os); os << nl;
pv_.writeData(os); os << nl;
hl_.writeData(os); os << nl;
Cp_.writeData(os); os << nl;
Cpg_.writeData(os); os << nl;
B_.writeData(os); os << nl;
mu_.writeData(os); os << nl;
mug_.writeData(os); os << nl;
K_.writeData(os); os << nl;
Kg_.writeData(os); os << nl;
sigma_.writeData(os); os << nl;
D_.writeData(os); os << endl;
}
//- Ostream Operator
friend Ostream& operator<<(Ostream& os, const C2H6& l)
{
l.writeData(os);
return os;
}
};
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
} // End namespace Foam
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
#include "C2H6I.H"
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
#endif
// ************************************************************************* //