/*
 * CoolPropFluid.h
 *
 *  Created on: 20 Dec 2013
 *      Author: jowr
 */

#ifndef COOLPROPFLUID_H_
#define COOLPROPFLUID_H_

#include "DataStructures.h"
#include "Helmholtz.h"
#include "Solvers.h"

#include <numeric>
#include <string>
#include <vector>
#include <map>
#include <assert.h>
#include <iterator>
#include "Eigen/Core"
#include "PolyMath.h"

namespace CoolProp {

struct BibTeXKeysStruct
{
    std::string EOS,
                CP0,
                VISCOSITY,
                CONDUCTIVITY,
                ECS_LENNARD_JONES,
                ECS_FITS,
                SURFACE_TENSION;
};

struct EnvironmentalFactorsStruct
{
    double GWP20, GWP100, GWP500, ODP, HH, PH, FH;
    std::string ASHRAE34;
};

/// A set of limits for the eos parameters
struct EOSLimits
{
    double Tmin, Tmax, rhomax, pmax;
};

struct ConductivityECSVariables{
    std::string reference_fluid;
    long double psi_rhomolar_reducing, f_int_T_reducing;
    std::vector<long double> psi_a, psi_t, f_int_a, f_int_t;
};

struct ConductivityDiluteEta0AndPolyData{
    std::vector<long double> A, t;
};

struct ConductivityDiluteRatioPolynomialsData{
    long double T_reducing, p_reducing;
    std::vector<long double> A, B, n, m;
};
struct ConductivityDiluteVariables
{
    enum ConductivityDiluteEnum {CONDUCTIVITY_DILUTE_RATIO_POLYNOMIALS,
                                 CONDUCTIVITY_DILUTE_ETA0_AND_POLY,
                                 CONDUCTIVITY_DILUTE_CO2,
                                 CONDUCTIVITY_DILUTE_ETHANE,
                                 CONDUCTIVITY_DILUTE_NONE,
                                 CONDUCTIVITY_DILUTE_NOT_SET
                                 };
    int type;
    ConductivityDiluteRatioPolynomialsData ratio_polynomials;
    ConductivityDiluteEta0AndPolyData eta0_and_poly;

    ConductivityDiluteVariables(){type = CONDUCTIVITY_DILUTE_NOT_SET;}
};

struct ConductivityResidualPolynomialAndExponentialData{
    long double T_reducing, rhomass_reducing;
    std::vector<long double> A, t, d, gamma, l;
};

struct ConductivityResidualPolynomialData{
    long double T_reducing, rhomass_reducing;
    std::vector<long double> B, t, d;
};
struct ConductivityResidualVariables
{
    enum ConductivityResidualEnum {CONDUCTIVITY_RESIDUAL_POLYNOMIAL,
                                   CONDUCTIVITY_RESIDUAL_POLYNOMIAL_AND_EXPONENTIAL,
                                   CONDUCTIVITY_RESIDUAL_R123,
                                   CONDUCTIVITY_RESIDUAL_CO2,
                                   CONDUCTIVITY_RESIDUAL_NOT_SET
                                   };
    int type;
    ConductivityResidualPolynomialData polynomials;
    ConductivityResidualPolynomialAndExponentialData polynomial_and_exponential;

    ConductivityResidualVariables(){type = CONDUCTIVITY_RESIDUAL_NOT_SET;}
};

struct ConductivityCriticalSimplifiedOlchowySengersData{
    long double T_reducing, p_reducing, k, R0, gamma, nu, qD, zeta0, GAMMA, T_ref;
    ConductivityCriticalSimplifiedOlchowySengersData(){
        // Universal constants - can still be adjusted if need be
        k = 1.3806488e-23; //[J/K]
        R0 = 1.03; //[-]
		gamma = 1.239; //[-]
		nu = 0.63; //[-]
        // Suggested default values - can be over-written
        GAMMA = 0.0496; //[-]
        zeta0 = 1.94e-10; //[m]
        qD = 2e9; //[m]

        // Set to invalid number, can be provided in the JSON file
        // Default is 1.5*Tc
        T_ref = _HUGE;
    }
};
struct ConductivityCriticalVariables
{
    enum ConductivityResidualEnum {CONDUCTIVITY_CRITICAL_SIMPLIFIED_OLCHOWY_SENGERS,
                                   CONDUCTIVITY_CRITICAL_R123,
                                   CONDUCTIVITY_CRITICAL_AMMONIA,
                                   CONDUCTIVITY_CRITICAL_NONE,
                                   CONDUCTIVITY_CRITICAL_CARBONDIOXIDE_SCALABRIN_JPCRD_2006,
                                   CONDUCTIVITY_CRITICAL_NOT_SET
                                   };
    int type;
    ConductivityCriticalSimplifiedOlchowySengersData Olchowy_Sengers;

    ConductivityCriticalVariables(){type = CONDUCTIVITY_CRITICAL_NOT_SET; }
};

/// Variables for the dilute gas part
struct ViscosityDiluteGasCollisionIntegralData
{
    long double molar_mass, C;
    std::vector<long double> a, t;
};
struct ViscosityDiluteCollisionIntegralPowersOfTstarData
{
    long double T_reducing, C;
    std::vector<long double> a, t;
};
struct ViscosityDiluteGasPowersOfT
{
    std::vector<long double> a, t;
};
struct ViscosityDiluteVariables
{
    enum ViscosityDiluteEnum {VISCOSITY_DILUTE_COLLISION_INTEGRAL,
                              VISCOSITY_DILUTE_COLLISION_INTEGRAL_POWERS_OF_TSTAR,
                              VISCOSITY_DILUTE_KINETIC_THEORY,
                              VISCOSITY_DILUTE_ETHANE,
                              VISCOSITY_DILUTE_POWERS_OF_T,
                              VISCOSITY_DILUTE_NOT_SET
                              };
    int type;
    ViscosityDiluteGasCollisionIntegralData collision_integral;
    ViscosityDiluteCollisionIntegralPowersOfTstarData collision_integral_powers_of_Tstar;
    ViscosityDiluteGasPowersOfT powers_of_T;

    ViscosityDiluteVariables(){type = VISCOSITY_DILUTE_NOT_SET;}
};

struct ViscosityRainWaterFriendData
{
    std::vector<long double> b, t;
};
struct ViscosityInitialDensityVariables
{
    ViscosityRainWaterFriendData rainwater_friend;
};

struct ViscosityModifiedBatschinskiHildebrandData
{
    std::vector<long double> a,d1,d2,t1,t2,f,g,h,p,q,gamma, l;
    long double T_reduce, rhomolar_reduce;
};
struct ViscosityFrictionTheoryData
{
    std::vector<long double> Aa, Aaa, Aaaa, Ar, Arr, Adrdr, Arrr, Ai, Aii, AdrAdr;
    int Na, Naa, Naaa, Nr, Nrr, Nrrr, Nii;
    long double c1, c2, T_reduce, rhomolar_reduce;
};
struct ViscosityHigherOrderVariables
{
    enum ViscosityDiluteEnum {VISCOSITY_HIGHER_ORDER_BATSCHINKI_HILDEBRAND,
                              VISCOSITY_HIGHER_ORDER_HYDROGEN,
                              VISCOSITY_HIGHER_ORDER_HEXANE,
                              VISCOSITY_HIGHER_ORDER_HEPTANE,
                              VISCOSITY_HIGHER_ORDER_ETHANE,
                              VISCOSITY_HIGHER_ORDER_FRICTION_THEORY,
                              VISCOSITY_HIGHER_ORDER_NOT_SET
                              };
    int type;
    ViscosityModifiedBatschinskiHildebrandData modified_Batschinski_Hildebrand;
    ViscosityFrictionTheoryData friction_theory;
    ViscosityHigherOrderVariables(){type = VISCOSITY_HIGHER_ORDER_NOT_SET;};
};

struct ViscosityECSVariables{
    std::string reference_fluid;
    long double psi_rhomolar_reducing;
    std::vector<long double> psi_a, psi_t;
};

class TransportPropertyData
{
public:
    enum ViscosityDiluteEnum {VISCOSITY_HARDCODED_WATER,
                              VISCOSITY_HARDCODED_HELIUM,
                              VISCOSITY_HARDCODED_R23,
                              VISCOSITY_NOT_HARDCODED
                              };
    enum ConductivityDiluteEnum {
                                 CONDUCTIVITY_HARDCODED_WATER,
                                 CONDUCTIVITY_HARDCODED_R23,
                                 CONDUCTIVITY_HARDCODED_HELIUM,
                                 CONDUCTIVITY_NOT_HARDCODED
                                 };
    ViscosityDiluteVariables viscosity_dilute;
    ViscosityInitialDensityVariables viscosity_initial;
    ViscosityHigherOrderVariables viscosity_higher_order;
    ViscosityECSVariables viscosity_ecs;
    ConductivityDiluteVariables conductivity_dilute;
    ConductivityResidualVariables conductivity_residual;
    ConductivityCriticalVariables conductivity_critical;
    ConductivityECSVariables conductivity_ecs;

    std::string BibTeX_viscosity, BibTeX_conductivity;
    bool viscosity_using_ECS; ///< A flag for whether to use extended corresponding states for viscosity.  False for no
    bool conductivity_using_ECS; ///< A flag for whether to use extended corresponding states for conductivity.  False for no
    long double sigma_eta, epsilon_over_k;
    int hardcoded_viscosity, hardcoded_conductivity;
    TransportPropertyData(){hardcoded_viscosity = VISCOSITY_NOT_HARDCODED;
                            hardcoded_conductivity = CONDUCTIVITY_NOT_HARDCODED;
                            viscosity_using_ECS = false;
                            conductivity_using_ECS = false;
    };
};

/**
The surface tension correlation class uses correlations for the surface tension that are all
of the form

\f[
\sigma = \sum_{i=0}^{k-1}a_i\left(1-\frac{T}{\tilde T_c}\right)^{n_i}
\f]

where \f$ \tilde T_c \f$ is the critical temperature used for the correlation which is
almost always equal to the critical temperature of the equation of state.  Result for
surface tension is in N/m
*/
class SurfaceTensionCorrelation
{
public:
    std::vector<long double> a, n, s;
    long double Tc;

    std::size_t N;

    std::string BibTeX;
    SurfaceTensionCorrelation(){};
    SurfaceTensionCorrelation(rapidjson::Value &json_code)
    {
        a = cpjson::get_long_double_array(json_code["a"]);
        n = cpjson::get_long_double_array(json_code["n"]);

        Tc = cpjson::get_double(json_code,"Tc");
        BibTeX = cpjson::get_string(json_code,"BibTeX");

        this->N = n.size();
        s = n;
    };
    long double evaluate(long double T)
    {
        if (a.empty()){ throw NotImplementedError(format("surface tension curve not provided"));}
        long double THETA = 1-T/Tc;
        for (std::size_t i = 0; i < N; ++i)
        {
            s[i] = a[i]*pow(THETA, n[i]);
        }
        return std::accumulate(s.begin(), s.end(), 0.0);
    }
};
/**
*/
class SaturationAncillaryFunction
{
private:
    Eigen::MatrixXd num_coeffs, ///< Coefficients for numerator in rational polynomial 
                    den_coeffs; ///< Coefficients for denominator in rational polynomial
    std::vector<double> n, t, s;
    bool using_tau_r;
    long double Tmax, Tmin, reducing_value, T_r, max_abs_error;
    int type;
    enum ancillaryfunctiontypes{TYPE_NOT_SET = -1, TYPE_NOT_EXPONENTIAL = 0, TYPE_EXPONENTIAL = 1, TYPE_RATIONAL_POLYNOMIAL = 2};
    std::size_t N;
public:

    SaturationAncillaryFunction(){type = TYPE_NOT_SET;};
    
    SaturationAncillaryFunction(rapidjson::Value &json_code)
    {
        std::string type = cpjson::get_string(json_code,"type");
        if (!type.compare("rational_polynomial"))
        {
            num_coeffs = vec_to_eigen(cpjson::get_double_array(json_code["A"]));
            den_coeffs = vec_to_eigen(cpjson::get_double_array(json_code["B"]));
            max_abs_error = cpjson::get_double(json_code,"max_abs_error");
        }
        else
        {
            n = cpjson::get_double_array(json_code["n"]);
            t = cpjson::get_double_array(json_code["t"]);
            Tmin = cpjson::get_double(json_code,"Tmin");
            Tmax = cpjson::get_double(json_code,"Tmax");
            reducing_value = cpjson::get_double(json_code,"reducing_value");
            using_tau_r = cpjson::get_bool(json_code,"using_tau_r");
            T_r = cpjson::get_double(json_code,"T_r");    
        }   
        
        if (!type.compare("rational_polynomial"))
            this->type = TYPE_RATIONAL_POLYNOMIAL;
        else if (!type.compare("rhoLnoexp"))
            this->type = TYPE_NOT_EXPONENTIAL;
        else
            this->type = TYPE_EXPONENTIAL;
        this->N = n.size();
        s = n;
    };
    
    /// Get the maximum absolute error for this fit
    long double get_max_abs_error(){return max_abs_error;};
    
    double evaluate(double T)
    {
        if (type == TYPE_NOT_SET)
        {
            throw ValueError(format("type not set"));
        }
        else if (type == TYPE_RATIONAL_POLYNOMIAL)
        {
            Polynomial2D poly;
            return poly.evaluate(num_coeffs, T)/poly.evaluate(den_coeffs, T);
        }
        else
        {
            double THETA = 1-T/T_r;

            for (std::size_t i = 0; i < N; ++i)
            {
                s[i] = n[i]*pow(THETA, t[i]);
            }
            double summer = std::accumulate(s.begin(), s.end(), 0.0);

            if (type == TYPE_NOT_EXPONENTIAL)
            {
                return reducing_value*(1+summer);
            }
            else
            {
                double tau_r_value;
                if (using_tau_r)
                    tau_r_value = T_r/T;
                else
                    tau_r_value = 1.0;
                return reducing_value*exp(tau_r_value*summer);
            }
        }
    }
    double invert(double value)
    {
        // Invert the ancillary curve to get the temperature as a function of the output variable
        // Define the residual to be driven to zero
        class solver_resid : public FuncWrapper1D
        {
        public:
            int other;
            SaturationAncillaryFunction *anc;
            long double T, value, r, current_value;

            solver_resid(SaturationAncillaryFunction *anc, long double value) : anc(anc), value(value){};

            double call(double T){
                this->T = T;
                current_value = anc->evaluate(T);
                r = current_value - value;
                return r;
            };
        };
        solver_resid resid(this, value);
        std::string errstring;

        return Brent(resid,Tmin,Tmax,DBL_EPSILON,1e-12,100,errstring);
    }
};

struct MeltingLinePiecewiseSimonSegment
{
    long double T_0, a, c, p_0, T_max, T_min;
};
struct MeltingLinePiecewiseSimonData
{
    std::vector<MeltingLinePiecewiseSimonSegment> parts;
};
struct MeltingLinePiecewisePolynomialInTrSegment
{
    std::vector<long double> a, t;
    long double T_0, p_0, T_max, T_min;
};
struct MeltingLinePiecewisePolynomialInTrData
{
    std::vector<MeltingLinePiecewisePolynomialInTrSegment> parts;
};
struct MeltingLinePiecewisePolynomialInThetaSegment
{
    std::vector<long double> a, t;
    long double T_0, p_0, T_max, T_min;
};
struct MeltingLinePiecewisePolynomialInThetaData
{
    std::vector<MeltingLinePiecewisePolynomialInThetaSegment> parts;
};
class MeltingLineVariables
{
public:
    enum MeltingLineVariablesEnum{
        MELTING_LINE_SIMON_TYPE,
        MELTING_LINE_POLYNOMIAL_IN_TR_TYPE,
        MELTING_LINE_POLYNOMIAL_IN_THETA_TYPE,
        MELTING_LINE_NOT_SET
    };
    long double evaluate(int OF, int GIVEN, long double value)
    {
        if (type == MELTING_LINE_NOT_SET){throw ValueError("Melting line curve not set");}
        if (OF == iP && GIVEN == iT){
            long double T = value;
            if (type == MELTING_LINE_SIMON_TYPE){
                // Need to find the right segment
                for (std::size_t i = 0; i < simon.parts.size(); ++i){
                    MeltingLinePiecewiseSimonSegment &part = simon.parts[i];
                    if (T >= part.T_min && T <= part.T_max){
                        return part.p_0 + part.a*(pow(T/part.T_0,part.c)-1);
                    }
                }
                throw ValueError("unable to calculate melting line (p,T) for Simon curve");
            }
            else if (type == MELTING_LINE_POLYNOMIAL_IN_TR_TYPE){
                // Need to find the right segment
                for (std::size_t i = 0; i < polynomial_in_Tr.parts.size(); ++i){
                    MeltingLinePiecewisePolynomialInTrSegment &part = polynomial_in_Tr.parts[i];
                    if (T >= part.T_min && T <= part.T_max){
                        long double summer = 0;
                        for (std::size_t i =0; i < part.a.size(); ++i){
                            summer += part.a[i]*(pow(T/part.T_0,part.t[i])-1);
                        }
                        return part.p_0*(1+summer);
                    }
                }
                throw ValueError("unable to calculate melting line (p,T) for polynomial_in_Tr curve");
            }
            else if (type == MELTING_LINE_POLYNOMIAL_IN_THETA_TYPE){
                // Need to find the right segment
                for (std::size_t i = 0; i < polynomial_in_Theta.parts.size(); ++i){
                    MeltingLinePiecewisePolynomialInThetaSegment &part = polynomial_in_Theta.parts[i];
                    if (T >= part.T_min && T <= part.T_max){
                        long double summer = 0;
                        for (std::size_t i =0; i < part.a.size(); ++i){
                            summer += part.a[i]*pow(T/part.T_0-1,part.t[i]);
                        }
                        return part.p_0*(1+summer);
                    }
                }
                throw ValueError("unable to calculate melting line (p,T) for polynomial_in_Theta curve");
            }
            else{
                throw ValueError("only Simon supported now");
            }
        }
        else{
            throw ValueError("only melt(P,T) supported now");
        }
    }
    std::string BibTeX;
    long double T_m; ///< Melting temperature at 1 atmosphere
    MeltingLinePiecewiseSimonData simon;
    MeltingLinePiecewisePolynomialInTrData polynomial_in_Tr;
    MeltingLinePiecewisePolynomialInThetaData polynomial_in_Theta;
    int type;
    MeltingLineVariables(){type = MELTING_LINE_NOT_SET;};
};

struct Ancillaries
{
    SaturationAncillaryFunction pL, pV, rhoL, rhoV, hL, hLV, sL, sLV;
    MeltingLineVariables melting_line;
    SurfaceTensionCorrelation surface_tension;
};

/// The core class for an equation of state
/**
 This class holds the absolute minimum information to evaluate the equation
 of state.  This includes the reducing state, limits on the equation of state,
 the coefficients for the Helmholtz derivative terms.

 It does NOT include derived parameters like specific heat, enthalpy, etc.
*/
class EquationOfState{
public:
    EquationOfState(){};
    ~EquationOfState(){};
    SimpleState reduce, ///< Reducing state used for the EOS (usually, but not always, the critical point)
                sat_min_liquid, ///< The saturated liquid state at the minimum saturation temperature
                sat_min_vapor, ///< The saturated vapor state at the minimum saturation temperature
                hs_anchor; ///< A fixed anchor state at Tc*1.1 and rhoc*0.9 used as a reference state for enthalpy and entropy ancillary curves
    EOSLimits limits; ///< Limits on the EOS
    double R_u, ///< The universal gas constant used for this EOS (usually, but not always, 8.314472 J/mol/K)
           molar_mass, ///< The molar mass in kg/mol (note NOT kg/kmol)
           accentric, ///< The accentric factor \f$ \omega = -log_{10}\left(\frac{p_s(T/T_c=0.7)}{p_c}\right)-1\f$
           Ttriple, ///< Triple point temperature (K)
           ptriple; ///< Triple point pressure (Pa)
    bool pseudo_pure; ///< Is a pseudo-pure fluid (true) or pure fluid (false)
    ResidualHelmholtzContainer alphar; ///< The residual Helmholtz energy
    IdealHelmholtzContainer alpha0; ///< The ideal Helmholtz energy
    std::string BibTeX_EOS, ///< The bibtex key for the equation of state
                BibTeX_CP0; ///< The bibtex key for the ideal gas specific heat correlation

    /// Validate the EOS that was just constructed
    void validate()
    {
        assert(R_u < 9 && R_u > 8);
        assert(molar_mass > 0.001 && molar_mass < 1);
    };
    long double baser(const long double &tau, const long double &delta) throw()
    {
        return alphar.base(tau, delta);
    };
    // First partials
    long double dalphar_dDelta(const long double &tau, const long double &delta) throw()
    {
        return alphar.dDelta(tau, delta);
    };
    long double dalphar_dTau(const long double &tau, const long double &delta) throw()
    {
        return alphar.dTau(tau, delta);
    };
    // Second partials
    long double d2alphar_dDelta2(const long double &tau, const long double &delta) throw()
    {
        return alphar.dDelta2(tau, delta);
    };
    long double d2alphar_dDelta_dTau(const long double &tau, const long double &delta) throw()
    {
        return alphar.dDelta_dTau(tau, delta);
    };
    long double d2alphar_dTau2(const long double &tau, const long double &delta) throw()
    {
        return alphar.dTau2(tau, delta);
    };
    // Third partials
    long double d3alphar_dDelta3(const long double &tau, const long double &delta) throw()
    {
        return alphar.dDelta3(tau, delta);
    };
    long double d3alphar_dDelta2_dTau(const long double &tau, const long double &delta) throw()
    {
        return alphar.dDelta2_dTau(tau, delta);
    };
    long double d3alphar_dDelta_dTau2(const long double &tau, const long double &delta) throw()
    {
        return alphar.dDelta_dTau2(tau, delta);
    };
    long double d3alphar_dTau3(const long double &tau, const long double &delta) throw()
    {
        return alphar.dTau3(tau, delta);
    };


    long double base0(const long double &tau, const long double &delta) throw()
    {
        return alpha0.base(tau, delta);
    };
    // First partials
    long double dalpha0_dDelta(const long double &tau, const long double &delta) throw()
    {
        return alpha0.dDelta(tau, delta);
    };
    long double dalpha0_dTau(const long double &tau, const long double &delta) throw()
    {
        return alpha0.dTau(tau, delta);
    };
    // Second partials
    long double d2alpha0_dDelta2(const long double &tau, const long double &delta) throw()
    {
        return alpha0.dDelta2(tau, delta);
    };
    long double d2alpha0_dDelta_dTau(const long double &tau, const long double &delta) throw()
    {
        return alpha0.dDelta_dTau(tau, delta);
    };
    long double d2alpha0_dTau2(const long double &tau, const long double &delta) throw()
    {
        return alpha0.dTau2(tau, delta);
    };
    // Third partials
    long double d3alpha0_dDelta3(const long double &tau, const long double &delta) throw()
    {
        return alpha0.dDelta3(tau, delta);
    };
    long double d3alpha0_dDelta2_dTau(const long double &tau, const long double &delta) throw()
    {
        return alpha0.dDelta2_dTau(tau, delta);
    };
    long double d3alpha0_dDelta_dTau2(const long double &tau, const long double &delta) throw()
    {
        return alpha0.dDelta_dTau2(tau, delta);
    };
    long double d3alpha0_dTau3(const long double &tau, const long double &delta) throw()
    {
        return alpha0.dTau3(tau, delta);
    };
};

/// A thermophysical property provider for critical and reducing values as well as derivatives of Helmholtz energy
/**
This fluid instance is populated using an entry from a JSON file
*/
class CoolPropFluid {
    protected:
        // Transport property data
        std::string ECSReferenceFluid; ///< A string that gives the name of the fluids that should be used for the ECS method for transport properties
        double ECS_qd; ///< The critical qd parameter for the Olchowy-Sengers cross-over term
    public:
        CoolPropFluid(){};
        ~CoolPropFluid(){};
        EquationOfState *pEOS; ///< A pointer to the currently used EOS
        std::vector<EquationOfState> EOSVector; ///< The equations of state that could be used for this fluid

        std::string name; ///< The name of the fluid
        std::string REFPROPname; ///< The REFPROP-compliant name if REFPROP-"name" is not a compatible fluid name.  If not included, "name" is assumed to be a valid name for REFPROP
        std::string CAS; ///< The CAS number of the fluid
        std::vector <std::string> aliases; ///< A vector of aliases of names for the fluid

        BibTeXKeysStruct BibTeXKeys;
        EnvironmentalFactorsStruct environment;
        Ancillaries ancillaries;
        TransportPropertyData transport;
        SimpleState crit, ///< The state at the critical point
                    triple_liquid, ///< The saturated liquid state at the triple point temperature
                    triple_vapor; ///< The saturated vapor state at the triple point temperature

        double gas_constant(){ return pEOS->R_u; };
        double molar_mass(){ return pEOS->molar_mass; };
};


} /* namespace CoolProp */
#endif /* COOLPROPFLUID_H_ */