/* 
Properties for R407C.  
by Ian Bell (ihb2@cornell.edu)

Pseudo-pure fluid thermo props from 
"Pseudo-pure fluid Equations of State for the Refrigerant Blends R410A, R407C, R507C and R407C" 
by E.W. Lemmon, Int. J. Thermophys. v. 24, n4, 2003

*/

#if defined(_MSC_VER)
#define _CRTDBG_MAP_ALLOC
#define _CRT_SECURE_NO_WARNINGS
#include <stdlib.h>
#include <crtdbg.h>
#else
#include <stdlib.h>
#endif

#include "math.h"
#include "stdio.h"
#include <string.h>
#include "CoolProp.h"
#include "FluidClass.h"
#include "R407C.h"

static const double a[]={
    2.13194,		//[0]
    8.05008,		//[1]
    -14.3914,		//[2]
    1.4245,			//[3]
    3.9419,			//[4]
    3.1209			//[5]
};

static const double b[]={
    0,				//[0]
    0,				//[1]
    -0.4,			//[2]
    2.40437,		//[3]
    5.25122,		//[4]
    13.3632			//[5]
};

static const double N[]={
	 0.0,			//[0]
	 1.0588,		//[1]
	-1.12018,		//[2]
	 0.629064,		//[3]
	-0.351953,		//[4]
	 0.00455978,	//[5]
	-1.75725,		//[6]
	-1.12009,		//[7]
	 0.0277353,		//[8]
	 0.898881,		//[9]
	-1.17591,		//[10]
	 0.0818591,		//[11]
	-0.0794097,		//[12]
	-0.0000104047,	//[13]
	 0.233779,		//[14]
	-0.291790,		//[15]
	 0.0154776,		//[16]
	-0.0314579,		//[17]
	-0.00442552,	//[18]
	-0.0101254,		//[19]
	 0.00915953,	//[20]
	-0.003615		//[21]
};

static const double t[]={
	0.0,			//[0]
    0.241,			//[1]
    0.69,			//[2]
    2.58,			//[3]
    1.15,			//[4]
    0.248,			//[5]
    2.15,			//[6]
    2.43,			//[7]
    5.3,			//[8]
    0.76,			//[9]
    1.48,			//[10]
    0.24,			//[11]
    2.86,			//[12]
    8.0,			//[13]
    3.3,			//[14]
    4.7,			//[15]
    0.45,			//[16]
    8.4,			//[17]
    16.2,			//[18]
    26.0,			//[19]
    16.0,			//[20]
    8.7				//[21]
};

static const int d[]={
	0,				//[0]
    1,				//[1]
    1,				//[2]
    1,				//[3]
    2,				//[4]
    5,				//[5]
    1,				//[6]
    2,				//[7]
    2,				//[8]
    3,				//[9]
    3,				//[10]
    5,				//[11]
    5,				//[12]
    5,				//[13]
    1,				//[14]
    1,				//[15]
    4,				//[16]
    4,				//[17]
    2,				//[18]
    4,				//[19]
    5,				//[20]
    6				//[21]
};

static const int l[]={
    0,				//[0]
	0,				//[1]
    0,				//[2]
    0,				//[3]
    0,				//[4]
    0,				//[5]
    1,				//[6]
    1,				//[7]
    1,				//[8]
    1,				//[9]
    1,				//[10]
    1,				//[11]
    1,				//[12]
    1,				//[13]
    2,				//[14]
    2,				//[15]
    2,				//[16]
    2,				//[17]
    3,				//[18]
    3,				//[19]
    3,				//[20]
    3				//[21]
};

static const double Nbp[]={
	0.0,			//[0]
	0.48722,		//[1]
    -6.6959,		//[2]
    -1.4165,		//[3]
    -2.5109			//[4]
};
    
static const double tbp[]={
	0.0,			//[0]
    0.54,			//[1]
    0.925,			//[2]
    2.7,			//[3]
    4.7				//[4]
};

static const double Ndp[]={
    0.0,			//[0]
	-0.086077,		//[1]
    -6.6364,		//[2]
    -2.4648,		//[3]
    -3.4776			//[4]
};

static const double tdp[]={
	0.0,			//[0]
    0.4,			//[1]
    0.965,			//[2]
    3.1,			//[3]
    5.0				//[4]
};



R407CClass::R407CClass()
{
	std::vector<double> n_v(N,N+sizeof(N)/sizeof(double));
	std::vector<double> d_v(d,d+sizeof(d)/sizeof(int));
	std::vector<double> t_v(t,t+sizeof(t)/sizeof(double));
	std::vector<double> l_v(l,l+sizeof(l)/sizeof(int));
	std::vector<double> a0(a,a+sizeof(a)/sizeof(double));
	std::vector<double> n0(b,b+sizeof(b)/sizeof(double));

	phi_BC * phir_ = new phir_power(n_v,d_v,t_v,l_v,1,21);
	phirlist.push_back(phir_);

	/*
	sum=log(delta)-log(tau)+a[0]+a[1]*tau+a[2]*pow(tau,b[2]);
	for(k=3;k<=5;k++)
	{
		sum+=a[k]*log(1.0-exp(-b[k]*tau));
	}
	*/
	phi_BC * phi0_lead_ = new phi0_lead(a0[0],a0[1]);
	phi_BC * phi0_logtau_ = new phi0_logtau(-1.0);
	phi_BC * phi0_power_ = new phi0_power(a0[2],n0[2]);
	phi_BC * phi0_Planck_Einstein_ = new phi0_Planck_Einstein(a0,n0,3,5);

	phi0list.push_back(phi0_lead_);
	phi0list.push_back(phi0_logtau_);
	phi0list.push_back(phi0_power_);
	phi0list.push_back(phi0_Planck_Einstein_);

	// Critical parameters (max condensing temperature)
	crit.rho = 453.43094;
	crit.p = 4631.7;
	crit.T = 359.345;
	crit.v = 1.0/crit.rho;

	// Other fluid parameters
	params.molemass = 86.2036;
	params.Ttriple = 200.0;
	params.ptriple = 11.3123436377;
	params.accentricfactor = 0.363;
	params.R_u = 8.314472;
	isPure = false;

	// Limits of EOS
	limits.Tmin = params.Ttriple;
	limits.Tmax = 500.0;
	limits.pmax = 50000.0;
	limits.rhomax = 17.04*params.molemass;
	
	EOSReference.assign("E.W. Lemmon, \"Pseudo-pure fluid Equations of State for the Refrigerant Blends R410A, R404A, R507C and R407C\"" 
						",Int. J. Thermophys. v. 24, n4, 2003");
	TransportReference.assign("Viscosity: V. Geller, \"Viscosity of Mixed Refrigerants R404A,R407C,"
							"R410A, and R507A\", 2000 Purdue Refrigeration conferences\n\n"
							"Thermal Conductivity: V.Z. Geller, B.Z. Nemzer, and U.V. Cheremnykh \"Thermal Conductivity "
							"of the Refrigerant mixtures R404A,R407C,R410A, and R507A\" "
							"Int. J. Thermophysics, v. 22, n 4 2001\n\n"
							"Surface Tension: R. Heide, \"The surface tension of HFC refrigerants and mixtures\", Int J. Refrig. Vol. 20, No. 7, pp. 496-503, 1997");

	name.assign("R407C");
	aliases.push_back("R407c");
}

double R407CClass::psatL(double T)
{
	//Bubble point of R410A
	double sum=0,theta;
	int k;
    theta=1-T/crit.T;
    
    for (k=1;k<=4;k++)
    {
        sum+=Nbp[k]*pow(theta,tbp[k]);
    }
    return reduce.p*exp(reduce.T/T*sum);
}
    
double R407CClass::psatV(double T)
{
	//Dew point of R410A
	double sum=0,theta;
	int k;
    theta=1-T/crit.T;

    for (k=1;k<=4;k++)
    {
        sum+=Ndp[k]*pow(theta,tdp[k]);
    }
    return reduce.p*exp(reduce.T/T*sum);
}

double R407CClass::rhosatV(double T)
{
	double theta;
	theta=1-T/359.345;
	return exp(+2.481666724+2.974063949110e+00*pow(theta,-0.023725)-14.334177672*theta+60.7010706462*theta*theta-376.514657192*powInt(theta,3)+1178.57631747*powInt(theta,4)-1999.37929072*powInt(theta,5)+1307.74729667*powInt(theta,6));
}

double R407CClass::rhosatL(double T)
{
	double theta;
	theta=1-T/359.345;
	return exp(5.544589249+1.764403419125e+00*pow(theta,0.12337)+0.544950396285*theta-0.784102758738*theta*theta+0.741332715649*theta*theta*theta);
}

double R407CClass::viscosity_Trho(double T, double rho)
{
    // Properties taken from "Viscosity of Mixed 
	// Refrigerants R407C,R407C,R410A, and R507A" 
	// by Vladimir Geller, 
	// 2000 Purdue Refrigeration conferences

    // inputs in T [K], and p [kPa]
    // output in Pa-s

   double eta_microPa_s;

   //Set constants required
   double a_0=-1.507e0,a_1=4.894e-2,a_2=-9.305e-6,b_1=-3.038e-3,b_2=2.927e-4,
	   b_3=-9.559e-7,b_4=1.739e-9,b_5=-1.455e-12,b_6=4.756e-16;

   eta_microPa_s=a_0+a_1*T+a_2*T*T+b_1*rho+b_2*rho*rho+b_3*rho*rho*rho+b_4*rho*rho*rho*rho+b_5*rho*rho*rho*rho*rho+b_6*rho*rho*rho*rho*rho*rho;
   return eta_microPa_s/1e6;
}

double R407CClass::conductivity_Trho(double T, double rho)
{
	// Properties taken from "Thermal Conductivity 
	// of the Refrigerant mixtures R407C,R407C,R410A, and R507A" 
	// by V.Z. Geller, B.Z. Nemzer, and U.V. Cheremnykh 
	// Int. J. Thermophysics, v. 22, n 4 2001

	// inputs in T [K], and p [kPa] or rho [kg/m^3]
	// output in W/m-K

	//Set constants required
	double a_0=-9.628e0,a_1=7.638e-2,b_1=2.715e-2,b_2=4.963e-5,b_3=-4.912e-8,b_4=2.884e-11;

	return (a_0+a_1*T+b_1*rho+b_2*rho*rho+b_3*rho*rho*rho+b_4*rho*rho*rho*rho)/1.e6; // from mW/m-K to kW/m-K
}
double R407CClass::surface_tension_T(double T)
{
	return 0.0583286*pow(1-T/reduce.T,1.237);
}