24Gamma=3.72992471469e-5,
32static const double Ameth[] = {
33 -7.25929210183, 4.13766054566e2, -6.32167316855e3,
34 3.34015577724e5, -1.68253379982e7, 1.87884851902e-2, -1.18673201223e1,
35 2.09062618015e3, -4.07532656958e5, -5.73917603241e-5,4.37711441593e-2,
36 -4.38766500673, 1.13524630779e-5, -5.07028240949e-5, 2.28002199522e-2,
37 9.25611329590e-9, 1.33865662546e-10, -1.65439044196e-7, 1.81030980110e-10,
38 5.45753645958e5, -3.63192281933e7, 4.81463473761, 1.56633022620e5,
39 7.89977010972e-5, 1.39993881210e-2, -1.70656092212e-11, -4.55256623445e-5,
40 -2.29314170748e-14,8.31548197665e-12, 6.84673626259e-20,
41 -4.70845544152e-17, 5.21465091383e-16
44static const double Dmeth[]=
45{ -1.78860165e-1, 4.83847500e-2, -1.84898700e-2 };
47static const double Fmeth[]=
48{ 4.77748580, 1.76065363, -5.67888940e-1, 1.32786231 };
50static const double Gmeth[]=
51{ 1.34740610e3, 1.35512060e2, -2.93910458e1, 2.12774600, 2.44656600e3 };
53double methane::C(
int i,
double rt,
double rt2)
57 return Ameth[0] * T + Ameth[1] * sqrt(T) + Ameth[2] + (Ameth[3] + Ameth[4] * rt) * rt;
59 return Ameth[5] * T + Ameth[6] + rt * (Ameth[7] + Ameth[8] * rt);
61 return Ameth[9] * T + Ameth[10] + Ameth[11] * rt;
65 return rt*(Ameth[13] + Ameth[14]*rt);
69 return rt*(Ameth[16] + Ameth[17]*rt);
73 return rt2*(Ameth[19] + Ameth[20]*rt);
75 return rt2*(Ameth[21] + Ameth[22]*rt2);
77 return rt2*(Ameth[23] + Ameth[24]*rt);
79 return rt2*(Ameth[25] + Ameth[26]*rt2);
81 return rt2*(Ameth[27] + Ameth[28]*rt);
83 return rt2*(Ameth[29] + Ameth[30]*rt + Ameth[31]*rt2);
89double methane::Cprime(
int i,
double rt,
double rt2,
double rt3)
93 return Ameth[0] + 0.5*Ameth[1]/sqrt(T) - (Ameth[3] + 2.0*Ameth[4]*rt)*rt2;
95 return Ameth[5] - rt2*(Ameth[7] + 2.0*Ameth[8]*rt);
97 return Ameth[9] - Ameth[11]*rt2;
101 return -rt2*(Ameth[13] + 2.0*Ameth[14]*rt);
103 return -Ameth[15]*rt2;
105 return -rt2*(Ameth[16] + 2.0*Ameth[17]*rt);
107 return -2.0*Ameth[18]*rt3;
109 return -rt3*(2.0*Ameth[19] + 3.0*Ameth[20]*rt);
111 return -rt3*(2.0*Ameth[21] + 4.0*Ameth[22]*rt2);
113 return -rt3*(2.0*Ameth[23] + 3.0*Ameth[24]*rt);
115 return -rt3*(2.0*Ameth[25] + 4.0*Ameth[26]*rt2);
117 return -rt3*(2.0*Ameth[27] + 3.0*Ameth[28]*rt);
119 return -rt3*(2.0*Ameth[29] + 3.0*Ameth[30]*rt + 4.0*Ameth[31]*rt2);
125double methane::W(
int n,
double egrho)
127 return (n == 0 ? (1.0 - egrho)/(2.0*Gamma) :
128 (n*W(n-1, egrho) - 0.5*pow(Rho,2*n)*egrho)/Gamma);
131double methane::H(
int i,
double egrho)
133 return (i < 8 ? pow(Rho,i+2) : pow(Rho,2*i-13)*egrho);
136double methane::I(
int i,
double egrho)
138 return (i < 8 ? pow(Rho,i+1)/
double(i+1) : W(i-8, egrho));
146 double egrho = exp(-Gamma*Rho*Rho);
147 double t3 = pow(T,1.0/3.0);
150 for (
int i=0; i<14; i++) {
151 sum += (C(i, rt, rt2) - T*Cprime(i, rt, rt2, rt3))*I(i, egrho);
153 sum += T*(Gmeth[0] + 0.75*Gmeth[1]*t3 + 0.6*Gmeth[2]*t3*t3 + 0.5*Gmeth[3]*T)
154 + Gmeth[4]*beta/(exp(beta*rt) - 1.0) + u0;
155 return sum + m_energy_offset;
163 double egrho = exp(-Gamma*Rho*Rho);
164 double t3 = pow(T,1.0/3.0);
166 sum = s0 - R*log(Rho);
167 for (
int i=0; i<14; i++) {
168 sum -= Cprime(i, rt, rt2, rt3)*I(i, egrho);
170 sum += Gmeth[0]*log(T) + 3.0*Gmeth[1]*t3 + 1.5*Gmeth[2]*t3*t3 + Gmeth[3]*T
171 + Gmeth[4]*(beta*rt + beta*rt/(exp(beta*rt) - 1.0)
172 - log(exp(beta*rt) - 1.0));
173 return sum + m_entropy_offset;
180 double egrho = exp(-Gamma*Rho*Rho);
183 for (
int i=0; i<14; i++) {
184 P += C(i, rt, rt2)*H(i, egrho);
191 double x = (1.0 - Tt/T)/(1.0 - Tt/Tc);
193 if ((T < Tmn) || (T > Tc)) {
195 "Temperature out of range. T = {}", T);
197 result = Fmeth[0]*
x + Fmeth[1]*
x*
x + Fmeth[2]*
x*
x*
x +
198 Fmeth[3]*
x*pow(1-
x, alpha);
199 return exp(result)*Pt;
207 if ((T < Tmn) || (T > Tc)) {
209 "Temperature out of range. T = {}", T);
211 w = (Tc - T)/(Tc - Tt);
212 sum = Dmeth[0]*(1.0 - pow(w, 2.0/3.0)) + Dmeth[1]*(1.0 - pow(w, 4.0/3.0))
213 + Dmeth[2]*(1.0 - pow(w, 2));
214 result = pow(w,alpha1)*exp(sum);
Base class for exceptions thrown by Cantera classes.
double x()
Vapor mass fraction.
double Vcrit()
Critical specific volume [m^3/kg].
double Tmax()
Maximum temperature for which the equation of state is valid.
double Tmin()
Minimum temperature for which the equation of state is valid.
double MolWt()
Molecular weight [kg/kmol].
double sp()
Entropy of a single-phase state.
double Tcrit()
Critical temperature [K].
double Pcrit()
Critical pressure [Pa].
double Psat()
Saturation pressure. Equation S3 from Reynolds TPSI.
double ldens()
Liquid density. Equation D3 from Reynolds TPSI.
double up()
Internal energy of a single-phase state.
Namespace for the Cantera kernel.
Contains declarations for string manipulation functions within Cantera.