liquidMixtureProperties.H

Go to the documentation of this file.

/*---------------------------------------------------------------------------*\
  =========                 |
  \\      /  F ield         | OpenFOAM: The Open Source CFD Toolbox
   \\    /   O peration     | Website:  https://openfoam.org
    \\  /    A nd           | Copyright (C) 2011-2020 OpenFOAM Foundation
     \\/     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::liquidMixtureProperties
 
Description
    A mixture of liquids
 
    An example of a two component liquid mixture:
    \verbatim
        <parentDictionary>
        {
            H2O; // employ default coefficients
 
            C7H16
            {
                // ... user defined properties for C7H16
            }
        }
    \endverbatim
 
SourceFiles
    liquidMixtureProperties.C
 
See also
    Foam::liquidProperties
 
\*---------------------------------------------------------------------------*/
 
#ifndef liquidMixtureProperties_H
#define liquidMixtureProperties_H
 
#include "liquidProperties.H"
#include "PtrList.H"
#include "scalarField.H"
 
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
 
namespace Foam
{
 
/*---------------------------------------------------------------------------*\
                   Class liquidMixtureProperties Declaration
\*---------------------------------------------------------------------------*/
 
class liquidMixtureProperties
{
    // Private Data
 
        //- Maximum reduced temperature
        static const scalar TrMax;
 
        //- The names of the liquids
        List<word> components_;
 
        //- The liquid properties
        PtrList<liquidProperties> properties_;
 
 
public:
 
    // Constructors
 
        //- Construct from dictionary
        liquidMixtureProperties(const dictionary& dict);
 
        //- Construct copy
        liquidMixtureProperties(const liquidMixtureProperties& lm);
 
        //- Construct and return a clone
        virtual autoPtr<liquidMixtureProperties> clone() const
        {
            return autoPtr<liquidMixtureProperties>
            (
                new liquidMixtureProperties(*this)
            );
        }
 
 
    //- Destructor
    virtual ~liquidMixtureProperties()
    {}
 
 
    // Selectors
 
        //- Select construct from dictionary
        static autoPtr<liquidMixtureProperties> New(const dictionary&);
 
 
    // Member Functions
 
        //- Return the liquid names
        inline const List<word>& components() const
        {
            return components_;
        }
 
        //- Return the liquid properties
        inline const PtrList<liquidProperties>& properties() const
        {
            return properties_;
        }
 
        //- Return the number of liquids in the mixture
        inline label size() const
        {
            return components_.size();
        }
 
        //- Calculate the critical temperature of mixture
        scalar Tc(const scalarField& X) const;
 
        //- Invert the vapour pressure relationship to retrieve the boiling
        //  temperature of the mixture as a function of pressure
        scalar pvInvert(const scalar p, const scalarField& X) const;
 
        //- Return pseudocritical temperature according to Kay's rule
        scalar Tpc(const scalarField& X) const;
 
        //- Return pseudocritical pressure (modified Prausnitz and Gunn)
        scalar Ppc(const scalarField& X) const;
 
        //- Return pseudo triple point temperature (mole averaged formulation)
        scalar Tpt(const scalarField& X) const;
 
        //- Return mixture accentric factor
        scalar omega(const scalarField& X) const;
 
        //- Return the surface molar fractions
        scalarField Xs
        (
            const scalar p,
            const scalar Tg,
            const scalar Tl,
            const scalarField& Xg,
            const scalarField& Xl
        ) const;
 
        //- Calculate the mean molecular weight [kg/kmol]
        //  from mole fractions
        scalar W(const scalarField& X) const;
 
        //- Returns the mass fractions corresponding to the given mole fractions
        scalarField Y(const scalarField& X) const;
 
        //- Returns the mole fractions corresponding to the given mass fractions
        scalarField X(const scalarField& Y) const;
 
        //- Calculate the mixture density [kg/m^3]
        scalar rho
        (
            const scalar p,
            const scalar T,
            const scalarField& X
        ) const;
 
        //- Calculate the mixture vapour pressure [Pa]
        scalar pv
        (
            const scalar p,
            const scalar T,
            const scalarField& X
        ) const;
 
        //- Calculate the mixture latent heat [J/kg]
        scalar hl
        (
            const scalar p,
            const scalar T,
            const scalarField& X
        ) const;
 
        //- Calculate the mixture heat capacity [J/kg/K]
        scalar Cp
        (
            const scalar p,
            const scalar T,
            const scalarField& X
        ) const;
 
        //- Estimate mixture surface tension [N/m]
        scalar sigma
        (
            const scalar p,
            const scalar T,
            const scalarField& X
        ) const;
 
        //- Calculate the mixture viscosity [Pa s]
        scalar mu
        (
            const scalar p,
            const scalar T,
            const scalarField& X
        ) const;
 
        //- Estimate thermal conductivity  [W/m/K]
        //  Li's method, Eq. 10-12.27 - 10.12-19
        scalar kappa
        (
            const scalar p,
            const scalar T,
            const scalarField& X
        ) const;
 
        //- Vapour diffusivity [m^2/s]
        scalar D
        (
            const scalar p,
            const scalar T,
            const scalarField& X
        ) const;
};
 
 
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
 
} // End namespace Foam
 
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
 
#endif
 
// ************************************************************************* //