PengRobinsonGasI.H

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#include "PengRobinsonGas.H"
#include "mathematicalConstants.H"

// * * * * * * * * * * * * * Private Member Functions  * * * * * * * * * * * //

template<class Specie>
inline Foam::PengRobinsonGas<Specie>::PengRobinsonGas
(
    const Specie& sp,
    const scalar& Tc,
    const scalar& Vc,
    const scalar& Zc,
    const scalar& Pc,
    const scalar& omega
)
:
    Specie(sp),
    Tc_(Tc),
    Vc_(Vc),
    Zc_(Zc),
    Pc_(Pc),
    omega_(omega)
{}


// * * * * * * * * * * * * * * * * Constructors  * * * * * * * * * * * * * * //

template<class Specie>
inline Foam::PengRobinsonGas<Specie>::PengRobinsonGas
(
    const word& name,
    const PengRobinsonGas& pg
)
:
    Specie(name, pg),
    Tc_(pg.Tc_),
    Pc_(pg.Pc_),
    Vc_(pg.Vc_),
    Zc_(pg.Zc_),
    omega_(pg.omega_)
{}


template<class Specie>
inline Foam::autoPtr<Foam::PengRobinsonGas <Specie>>
Foam::PengRobinsonGas<Specie>::clone() const
{
    return autoPtr<PengRobinsonGas<Specie>>
    (
        new PengRobinsonGas<Specie>(*this)
    );
}


template<class Specie>
inline Foam::autoPtr<Foam::PengRobinsonGas<Specie>>
Foam::PengRobinsonGas<Specie>::New
(
    const dictionary& dict
)
{
    return autoPtr<PengRobinsonGas<Specie>>
    (
        new PengRobinsonGas<Specie>(dict)
    );
}


// * * * * * * * * * * * * * * * Member Functions  * * * * * * * * * * * * * //

template<class Specie>
inline Foam::scalar Foam::PengRobinsonGas<Specie>::rho
(
    scalar p,
    scalar T
) const
{
    const scalar Z = this->Z(p, T);
    return p/(Z*this->R()*T);
}


template<class Specie>
inline Foam::scalar Foam::PengRobinsonGas<Specie>::H(scalar p, scalar T) const
{
    const scalar Pr = p/Pc_;
    const scalar Tr = T/Tc_;
    const scalar B = 0.07780*Pr/Tr;
    const scalar kappa = 0.37464 + 1.54226*omega_ - 0.26992*sqr(omega_);
    const scalar alpha = sqr(1 + kappa*(1 - sqrt(Tr)));

    const scalar Z = this->Z(p, T);

    return
        this->R()
       *Tc_
       *(
           Tr*(Z - 1)
         - 2.078*(1 + kappa)*sqrt(alpha)
          *log((Z + 2.414*B)/(Z - 0.414*B))
        );
}


template<class Specie>
inline Foam::scalar Foam::PengRobinsonGas<Specie>::Cp(scalar p, scalar T) const
{
    const scalar Tr = T/Tc_;
    const scalar a = 0.45724*sqr(RR*Tc_)/Pc_;
    const scalar b = 0.07780*RR*Tc_/Pc_;
    const scalar kappa = 0.37464 + 1.54226*omega_ - 0.26992*sqr(omega_);
    const scalar alpha = sqr(1 + kappa*(1 - sqrt(Tr)));

    const scalar A = a*alpha*p/sqr(RR*T);
    const scalar B = b*p/(RR*T);

    const scalar Z = this->Z(p, T);

    const scalar ap = kappa*a*(kappa/Tc_ - (1 + kappa)/sqrt(T*Tc_));
    const scalar app = kappa*a*(1 + kappa)/(2*sqrt(pow3(T)*Tc_));

    const scalar M = (sqr(Z) + 2*B*Z - sqr(B))/(Z - B);
    const scalar N = ap*B/(b*RR);

    const scalar root2 = sqrt(2.0);

    return
    (
        app*(T/(2*root2*b))*log((Z + (root2 + 1)*B)/(Z - (root2 - 1)*B))
      + RR*sqr(M - N)/(sqr(M) - 2*A*(Z + B))
      - RR
    )/this->W();
}


template<class Specie>
inline Foam::scalar Foam::PengRobinsonGas<Specie>::S
(
    scalar p,
    scalar T
) const
{
    const scalar Pr = p/Pc_;
    const scalar Tr = T/Tc_;
    const scalar B = 0.07780*Pr/Tr;
    const scalar kappa = 0.37464 + 1.54226*omega_ - 0.26992*sqr(omega_);

    const scalar Z = this->Z(p, T);

    return
        this->R()
       *(
          - log(p/Pstd)
          + (
                log(Z - B)
              - 2.078*kappa*((1 + kappa)/sqrt(Tr) - kappa)
               *log((Z + 2.414*B)/(Z - 0.414*B))
            )
        );
}


template<class Specie>
inline Foam::scalar Foam::PengRobinsonGas<Specie>::psi
(
    scalar p,
    scalar T
) const
{
    const scalar Z = this->Z(p, T);

    return 1.0/(Z*this->R()*T);
}


template<class Specie>
inline Foam::scalar Foam::PengRobinsonGas<Specie>::Z
(
    scalar p,
    scalar T
) const
{
    const scalar Tr = T/Tc_;
    const scalar a = 0.45724*sqr(RR*Tc_)/Pc_;
    const scalar b = 0.07780*RR*Tc_/Pc_;
    const scalar kappa = 0.37464 + 1.54226*omega_ - 0.26992*sqr(omega_);
    const scalar alpha = sqr(1 + kappa*(1 - sqrt(Tr)));

    const scalar A = a*alpha*p/sqr(RR*T);
    const scalar B = b*p/(RR*T);

    const scalar a2 = B - 1;
    const scalar a1 = A - 2*B - 3*sqr(B);
    const scalar a0 = -A*B + sqr(B) + pow3(B);

    const scalar Q = (3*a1 - a2*a2)/9.0;
    const scalar Rl = (9*a2*a1 - 27*a0 - 2*a2*a2*a2)/54.0;

    const scalar Q3 = Q*Q*Q;
    const scalar D = Q3 + Rl*Rl;

    scalar root = -1;

    if (D <= 0)
    {
        const scalar th = ::acos(Rl/sqrt(-Q3));
        const scalar qm = 2*sqrt(-Q);
        const scalar r1 = qm*cos(th/3.0) - a2/3.0;
        const scalar r2 =
            qm*cos((th + 2*constant::mathematical::pi)/3.0) - a2/3.0;
        const scalar r3 =
            qm*cos((th + 4*constant::mathematical::pi)/3.0) - a2/3.0;

        root = max(r1, max(r2, r3));
    }
    else
    {
        // One root is real
        const scalar D05 = sqrt(D);
        const scalar S = pow(Rl + D05, 1.0/3.0);
        scalar Tl = 0;
        if (D05 > Rl)
        {
            Tl = -pow(mag(Rl - D05), 1.0/3.0);
        }
        else
        {
            Tl = pow(Rl - D05, 1.0/3.0);
        }

        root = S + Tl - a2/3.0;
    }

    return root;
}


template<class Specie>
inline Foam::scalar Foam::PengRobinsonGas<Specie>::CpMCv
(
    scalar p,
    scalar T
) const
{
    const scalar Tr = T/Tc_;
    const scalar a = 0.45724*sqr(RR*Tc_)/Pc_;
    const scalar b = 0.07780*RR*Tc_/Pc_;
    const scalar kappa = 0.37464 + 1.54226*omega_ - 0.26992*sqr(omega_);
    const scalar alpha = sqr(1 + kappa*(1 - sqrt(Tr)));

    const scalar A = alpha*a*p/sqr(RR*T);
    const scalar B = b*p/(RR*T);

    const scalar Z = this->Z(p, T);

    const scalar ap = kappa*a*(kappa/Tc_ - (1 + kappa)/sqrt(T*Tc_));
    const scalar M = (sqr(Z) + 2*B*Z - sqr(B))/(Z - B);
    const scalar N = ap*B/(b*RR);

    return this->R()*sqr(M - N)/(sqr(M) - 2*A*(Z + B));
}


// * * * * * * * * * * * * * * * Member Operators  * * * * * * * * * * * * * //

template<class Specie>
inline void Foam::PengRobinsonGas<Specie>::operator+=
(
    const PengRobinsonGas<Specie>& pg
)
{
    scalar Y1 = this->Y();
    Specie::operator+=(pg);

    if (mag(this->Y()) > SMALL)
    {
        Y1 /= this->Y();
        const scalar Y2 = pg.Y()/this->Y();

        Tc_ = Y1*Tc_ + Y2*pg.Tc_;
        Vc_ = Y1*Vc_ + Y2*pg.Vc_;
        Zc_ = Y1*Zc_ + Y2*pg.Zc_;
        Pc_ = RR*Zc_*Tc_/Vc_;
        omega_ = Y1*omega_ + Y2*pg.omega_;
    }
}


template<class Specie>
inline void Foam::PengRobinsonGas<Specie>::operator*=(const scalar s)
{
     Specie::operator*=(s);
}


// * * * * * * * * * * * * * * * Friend Operators  * * * * * * * * * * * * * //


template<class Specie>
Foam::PengRobinsonGas<Specie> Foam::operator+
(
    const PengRobinsonGas<Specie>& pg1,
    const PengRobinsonGas<Specie>& pg2
)
{
    Specie sp
    (
        static_cast<const Specie&>(pg1)
      + static_cast<const Specie&>(pg2)
    );

    if (mag(sp.Y()) < SMALL)
    {
        return PengRobinsonGas<Specie>
        (
            sp,
            pg1.Tc_,
            pg1.Vc_,
            pg1.Zc_,
            pg1.Pc_,
            pg1.omega_
        );
    }
    else
    {
        const scalar Y1 = pg1.Y()/sp.Y();
        const scalar Y2 = pg2.Y()/sp.Y();

        const scalar Tc = Y1*pg1.Tc_ + Y2*pg2.Tc_;
        const scalar Vc = Y1*pg1.Vc_ + Y2*pg2.Vc_;
        const scalar Zc = Y1*pg1.Zc_ + Y2*pg2.Zc_;

        return PengRobinsonGas<Specie>
        (
            sp,
            Tc,
            Vc,
            Zc,
            RR*Zc*Tc/Vc,
            Y1*pg1.omega_ + Y2*pg2.omega_
        );
    }
}


template<class Specie>
Foam::PengRobinsonGas<Specie> Foam::operator*
(
    const scalar s,
    const PengRobinsonGas<Specie>& pg
)
{
    return PengRobinsonGas<Specie>
    (
        s*static_cast<const Specie&>(pg),
        pg.Tc_,
        pg.Vc_,
        pg.Zc_,
        pg.Pc_,
        pg.omega_
    );
}


template<class Specie>
Foam::PengRobinsonGas<Specie> Foam::operator==
(
    const PengRobinsonGas<Specie>& pg1,
    const PengRobinsonGas<Specie>& pg2
)
{
    Specie sp
    (
        static_cast<const Specie&>(pg1)
     == static_cast<const Specie&>(pg2)
    );

    const scalar Y1 = pg1.Y()/sp.Y();
    const scalar Y2 = pg2.Y()/sp.Y();

    const scalar Tc = Y2*pg2.Tc_ - Y1*pg1.Tc_;
    const scalar Vc = Y2*pg2.Vc_ - Y1*pg1.Vc_;
    const scalar Zc = Y2*pg2.Zc_ - Y1*pg1.Zc_;

    return PengRobinsonGas<Specie>
    (
        sp,
        Tc,
        Vc,
        Zc,
        RR*Zc*Tc/Vc,
        Y2*pg2.omega_ - Y1*pg1.omega_
    );
}


// ************************************************************************* //