cantera/src/tpx/Heptane.cpp
Ray Speth fcf7edf694 Implement Sub::name and Sub::formula in the base class
Eliminates the need for redundant implementations in all the derived
classes. Also, make the return value a "const char*" to eliminate the dangerous
cast.
2014-04-14 18:36:32 +00:00

270 lines
6 KiB
C++

/**
* @file Heptane.cpp representation of substance Heptane.
*
* Values and functions are from "Thermodynamic Properties in SI" by W.C.
* Reynolds. AUTHOR: jrh@stanford.edu: GCEP, Stanford University
*/
#include "Heptane.h"
#include "cantera/base/stringUtils.h"
using namespace Cantera;
namespace tpx
{
// Heptane constants
static const double Tmn = 182.56; // [K] minimum temperature for which calculations are valid
static const double Tmx = 1000.0; // [K] maximum temperature for which calculations are valid
static const double Tc=537.68; // [K] critical temperature
static const double Roc=197.60; // [kg/m^3] critical density
static const double To=300; // [K] reference Temperature
static const double R=82.99504; // [J/(kg*K)] gas constant (for this substance)
static const double Gamma=9.611604E-6; // [??]
static const double u0=3.4058439E5; // [] internal energy at To
static const double s0=1.1080254E3; // [] entropy at To
static const double Tp=400; // [K] ??
static const double Pc=2.6199E6; // [Pa] critical pressure
static const double M=100.20; // [kg/kmol] molar density
// array Ahept is used by the function Pp
static const double Ahept[]= {
2.246032E-3,
2.082990E2,
5.085746E7,
3.566396E9,
1.622168E9,
1.065237E-5,
5.987922E-1,
7.736602,
1.929386E5,
5.291379E-9
};
// array F is used by Psat
static const double F[]= {
-7.2298764,
3.8607475E-1,
-3.4216472,
4.6274432E-1,
-9.7926124,
-4.2058094E1,
7.5468678E1,
3.1758992E2
};
// array D is used by the function ldens
static const double D[]= {
1.9760405E2,
8.9451237E2,
-1.1462908E3,
1.7996947E3,
-1.7250843E3,
9.7088329E2
};
// array G is used by the function sp
static const double G[]= {
1.1925213E5,
-7.7231363E2,
7.4463527,
-3.0888167E-3,
0.0,
0.0
};
double Heptane::C(int j,double Tinverse, double T2inverse, double T3inverse, double T4inverse)
{
switch (j) {
case 0 :
return Ahept[0] * R * T -
Ahept[1] -
Ahept[2] * T2inverse +
Ahept[3] * T3inverse -
Ahept[4] * T4inverse;
case 1 :
return Ahept[5] * R * T -
Ahept[6] -
Ahept[7] * Tinverse;
case 2 :
return Ahept[9] * (Ahept[6] + Ahept[7] * Tinverse);
case 3 :
return Ahept[8] * T2inverse;
default :
return 0.0;
}
}
inline double Heptane::Cprime(int j, double T2inverse, double T3inverse, double T4inverse)
{
switch (j) {
case 0 :
return Ahept[0] * R -
-2 * Ahept[2] * T3inverse +
-3 * Ahept[3] * T4inverse -
-4 * Ahept[4] * pow(T, -5.0);
case 1 :
return Ahept[5] * R -
-1 * Ahept[7] * T2inverse;
case 2 :
return Ahept[9] * (-1 * Ahept[7] * T2inverse);
case 3 :
return -2 * Ahept[8] * T3inverse;
default :
return 0.0;
}
}
inline double Heptane::I(int j, double ergho, double Gamma)
{
switch (j) {
case 0:
return Rho;
case 1:
return Rho * Rho / 2;
case 2:
return pow(Rho, 5.0)/ 5;
case 3:
return 1 / Gamma - (Gamma * Rho * Rho + 2) * ergho / (2 * Gamma);
default:
return 0.0;
}
}
double Heptane::H(int i, double egrho)
{
if (i < 2) {
return pow(Rho,i+2);
} else if (i == 2) {
return pow(Rho,6.0);
} else if (i == 3) {
return pow(Rho,3) * (1 + Gamma * Rho * Rho) * egrho;
} else {
return 0;
}
}
double Heptane::up()
{
double Tinverse = 1.0/T;
double T2inverse = pow(T, -2);
double T3inverse = pow(T, -3);
double T4inverse = pow(T, -4);
double egrho = exp(-Gamma*Rho*Rho);
double sum = 0.0;
int i;
for (i=1; i<=5; i++) {
sum += G[i]*(pow(T,i) - pow(To,i))/double(i);
}
sum += G[0]*log(T/To);
for (i=0; i<=6; i++) {
sum += (C(i, Tinverse, T2inverse, T3inverse, T4inverse) - T*Cprime(i,T2inverse, T3inverse, T4inverse))*I(i,egrho, Gamma);
}
sum += u0;
return sum + m_energy_offset;
}
double Heptane::sp()
{
double T2inverse = pow(T, -2);
double T3inverse = pow(T, -3);
double T4inverse = pow(T, -4);
double egrho = exp(-Gamma*Rho*Rho);
double sum = 0.0;
for (int i=2; i<=5; i++) {
sum += G[i]*(pow(T,i-1) - pow(To,i-1))/double(i-1);
}
sum += G[1]*log(T/To);
sum -= G[0]*(1.0/T - 1.0/To);
for (int i=0; i<=6; i++) {
sum -= Cprime(i,T2inverse, T3inverse, T4inverse)*I(i,egrho, Gamma);
}
sum += s0 - R*log(Rho);
return sum + m_entropy_offset;
}
double Heptane::Pp()
{
double Tinverse = pow(T,-1);
double T2inverse = pow(T, -2);
double T3inverse = pow(T, -3);
double T4inverse = pow(T, -4);
double egrho = exp(-Gamma*Rho*Rho);
double P = Rho*R*T;
for (int i=0; i<=3; i++) {
P += C(i,Tinverse, T2inverse, T3inverse, T4inverse)*H(i,egrho);
}
return P;
}
double Heptane::Psat()
{
double log, sum=0;
if ((T < Tmn) || (T > Tc)) {
throw TPX_Error("Heptane::Psat",
"Temperature out of range. T = " + fp2str(T));
}
for (int i=1; i<=8; i++) {
sum += F[i-1] * pow((T/Tp -1),double(i-1));
}
log = ((Tc/T)-1)*sum;
return exp(log)*Pc;
}
double Heptane::ldens()
{
double xx=1-(T/Tc), sum=0;
if ((T < Tmn) || (T > Tc)) {
throw TPX_Error("Heptane::ldens",
"Temperature out of range. T = " + fp2str(T));
}
for (int i=1; i<=6; i++) {
sum+=D[i-1]*pow(xx,double(i-1)/3.0);
}
return sum;
}
// The following functions allow users to get the properties of Heptane that
// are not dependent on the state
double Heptane::Tcrit()
{
return Tc;
}
double Heptane::Pcrit()
{
return Pc;
}
double Heptane::Vcrit()
{
return 1.0/Roc;
}
double Heptane::Tmin()
{
return Tmn;
}
double Heptane::Tmax()
{
return Tmx;
}
double Heptane::MolWt()
{
return M;
}
}