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hrefprop.cpp
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284 lines (273 loc) · 6.34 KB
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//// CPP programmed by;
// LI Minchao
// tech center of DBC
// chengdu,sichuan,China
// minchao_li@126.com
//This c program rewrote the demonstrates explicitly linking to the subroutines available in
// refprop.dll. You can call the subroutines the same way as in the refprop.xls. In order to
//link this code hrefprop.h must be available in the current directory. And PATH in
//hrefrop.h should first be definated the REFPROP path. You can also package it into a dll
//dynamic library to conveniently call the subroutines.
//
#include "stdafx.h"
#include "hrefprop.h"
#include "initialDLL.h"
#include "convertunit.h"
#include <string.h>
//_CompFlag 0£ºbulk 1:liquidphase 2:vapor phase
double MoleWeight(int _CompFlag)
{
double MolWt;
switch (_CompFlag)
{
case 0:
WMOLdll(x, MolWt);
break;
case 1:
WMOLdll(xliq, MolWt);
break;
case 2:
WMOLdll(xvap, MolWt);
break;
}
return MolWt;
}
double Temperature(char* _Unit)
{
return UnitConvertDef(t, 'T', _Unit, -1, 0);
}
double Pressure(char* _Unit)
{
return UnitConvertDef(p / 1000.0, 'P', _Unit, -1, 0);
}
double Density(char* _Unit)
{
return UnitConvertDef(d, 'D', _Unit, -1, MoleWeight(0));
}
double LiquidDensity(char* _Unit)
{
return UnitConvertDef(Dl, 'D', _Unit, -1, MoleWeight(1));
}
double VaporDensity(char* _Unit)
{
return UnitConvertDef(Dv, 'D', _Unit, -1, MoleWeight(2));
}
double Volume(char* _Unit)
{
return UnitConvertDef(d, 'D', _Unit, -1, MoleWeight(0));
}
double Energy(char* _Unit)
{
return UnitConvertDef(e, 'H', _Unit, -1, MoleWeight(0));
}
double Enthalpy(char* _Unit)
{
return UnitConvertDef(h, 'H', _Unit, -1, MoleWeight(0));
}
double LiquidEnthalpy(char* _Unit)
{
if (q < 0.0 || q > 1.0)
{
strcpy_s(herr, "Inputs are single phase");
THERMdll(t, d, x, p, e, h, s, Cvcalc, Cpcalc, w, hjt);
return UnitConvertDef(h, 'H', _Unit, -1, MoleWeight(0));
}
else
{
THERMdll(t, Dl, xliq, p, el, hl, sl, Cvl, Cpl, wl, hjt);
return UnitConvertDef(hl, 'H', _Unit, -1, MoleWeight(1));
}
}
double VaporEnthalpy(char* _Unit)
{
if (q < 0.0 || q > 1.0)
{
strcpy_s(herr, "Inputs are single phase");
THERMdll(t, d, x, p, e, h, s, Cvcalc, Cpcalc, w, hjt);
return UnitConvertDef(h, 'H', _Unit, -1, MoleWeight(0));
}
else
{
THERMdll(t, Dv, xvap, p, ev, hv, sv, Cvv, Cpv, wv, hjt);
return UnitConvertDef(hv, 'H', _Unit, -1, MoleWeight(2));
}
}
double Entropy(char* _Unit)
{
return UnitConvertDef(s, 'S', _Unit, -1, MoleWeight(0));
}
double LiquidEntropy(char* _Unit)
{
if (q < 0.0 || q > 1.0)
{
strcpy_s(herr, "Inputs are single phase");
THERMdll(t, d, x, p, e, h, s, Cvcalc, Cpcalc, w, hjt);
return UnitConvertDef(s, 'S', _Unit, -1, MoleWeight(0));
}
else
{
THERMdll(t, Dl, xliq, p, el, hl, sl, Cvl, Cpl, wl, hjt);
return UnitConvertDef(sl, 'S', _Unit, -1, MoleWeight(1));
}
}
double VaporEntropy(char* _Unit)
{
if (q < 0.0 || q > 1.0)
{
strcpy_s(herr, "Inputs are single phase");
THERMdll(t, d, x, p, e, h, s, Cvcalc, Cpcalc, w, hjt);
return UnitConvertDef(s, 'S', _Unit, -1, MoleWeight(0));
}
else
{
THERMdll(t, Dv, xvap, p, ev, hv, sv, Cvv, Cpv, wv, hjt);
return UnitConvertDef(sv, 'S', _Unit, -1, MoleWeight(2));
}
}
double Cp(char* _Unit)
{
return UnitConvertDef(Cpcalc, 'S', _Unit, -1, MoleWeight(0));
}
double Cv(char* _Unit)
{
return UnitConvertDef(Cvcalc, 'S', _Unit, -1, MoleWeight(0));
}
double SpeedOfSound(char* _Unit)
{
return UnitConvertDef(w, 'W', _Unit, -1, MoleWeight(0));
}
double LatentHeat(char* _Unit)
{
if (q < 0.0 || q > 1.0)
{
strcpy_s(herr, "Inputs are single phase");
THERMdll(t, d, x, p, e, h, s, Cvcalc, Cpcalc, w, hjt);
return 0;
}
else return VaporEnthalpy(_Unit) - LiquidEnthalpy(_Unit);
}
double VaporizationHeat(char* _Unit)
{
return LatentHeat(_Unit);
}
double LHV(char* _Unit)
{
double hg, hn;
HEATdll(t, d, x, hg, hn, ierr, herr, 255);
return UnitConvertDef(hg, 'H', _Unit, -1, MoleWeight(0));
}
double LLV(char* _Unit)
{
double hg, hn;
HEATdll(t, d, x, hg, hn, ierr, herr, 255);
return UnitConvertDef(hn, 'H', _Unit, -1, MoleWeight(0));
}
double GrossHeatingValue(char* _Unit)
{
return LHV(_Unit);
}
double NetHeatingValue(char* _Unit)
{
return LLV(_Unit);
}
double JouleThomson(char* _Unit)
{
THERMdll(t, d, x, p, e, h, s, Cvcalc, Cpcalc, w, hjt);
return UnitConvertDef(hjt*1000.0, 'J', _Unit, -1, 0);
}
double* MoleFraction()
{
return x;
}
double* LiquidMoleFraction()
{
return xliq;
}
double* VaporMoleFraction()
{
return xvap;
}
double Viscosity(char* _Unit)
{
TRNPRPdll(t, d, x, eta, tcx, ierr, herr, 255);
if (q > 0 && q < 1)
{
eta = -9999999;
strcpy_s(herr, "Not pure fluid.");
}
if (!eta) strcpy_s(herr, "Unable to calculate property");
return UnitConvertDef(eta*0.000001, 'U', _Unit, -1, MoleWeight(0));
}
double ThermalConductivity(char* _Unit)
{
TRNPRPdll(t, d, x, eta, tcx, ierr, herr, 255);
if (q > 0 && q < 1)
{
tcx = -9999999;
strcpy_s(herr, "Not pure fluid.");
}
return UnitConvertDef(tcx * 1000, 'K', _Unit, -1, MoleWeight(0));
}
double KinematicViscosity(char* _Unit)
{
TRNPRPdll(t, d, x, eta, tcx, ierr, herr, 255);
if (!eta)
{
strcpy_s(herr, "Unable to calculate property");
return 0;
}
if (q > 0 && q < 1)
{
tcx = -9999999;
strcpy_s(herr, "Not pure fluid.");
}
else
eta = eta / d / MoleWeight(0) / 1000000;//m^2/s
return UnitConvertDef(eta, 'I', _Unit, -1, MoleWeight(0));
}
double Prandtl(char* _Unit)
{
TRNPRPdll(t, d, x, eta, tcx, ierr, herr, 255);
if (q > 0 && q < 1)
{
strcpy_s(herr, "Not pure fluid.");
return 0;
}
if (tcx == 0 || eta == 0)
{
strcpy_s(herr, "Unable to calculate property");
return 0;
}
THERMdll(t, d, x, p, e, h, s, Cvcalc, Cpcalc, w, hjt);
return eta * Cpcalc / tcx / MoleWeight(0) / 1000;
}
double SurfaceTension(char* _Unit)
{
double sigma;
if (q >= 0 && q <= 1)
{
SURFTdll(t, Dl, xliq, sigma, ierr, herr, 255);
wm = MoleWeight(1);
}
else
{
SURFTdll(t, d, x, sigma, ierr, herr, 255);
wm = MoleWeight(0);
}
return UnitConvertDef(sigma, 'N', _Unit, -1, wm);
}
double DielectricConstant(char* _Unit)
{
if (q > 0 && q < 1)
{
strcpy_s(herr, "Undefined");
return 0;
}
if (!t)
{
strcpy_s(herr, "Inputs out of range");
return 0;
}
DIELECdll(t, d, x, de);
return de;
}