Cantera  3.1.0b1
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Methane.cpp
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1//! @file Methane.cpp
2
3// This file is part of Cantera. See License.txt in the top-level directory or
4// at https://cantera.org/license.txt for license and copyright information.
5
6#include "Methane.h"
8
9using namespace Cantera;
10
11namespace tpx
12{
13static const double
14M = 16.04996,
15Tmn = 90.68,
16Tmx = 1700.0,
17Tc = 190.555,
18Pc = 4.5988e6,
19Roc= 160.43,
20Tt = 90.68,
21Pt=11743.5675,
22R = 5.18253475866e2,
23Gamma=3.72992471469e-5,
24alpha = 1.5, //Used with Psat
25alpha1 = .36, //used with ldens;
26Rot=451.562,
27beta=2009.152,
28u0 = 357696.0858,
29s0 = -1918.035071;
30
31static const double Ameth[] = {
32 -7.25929210183, 4.13766054566e2, -6.32167316855e3,
33 3.34015577724e5, -1.68253379982e7, 1.87884851902e-2, -1.18673201223e1,
34 2.09062618015e3, -4.07532656958e5, -5.73917603241e-5,4.37711441593e-2,
35 -4.38766500673, 1.13524630779e-5, -5.07028240949e-5, 2.28002199522e-2,
36 9.25611329590e-9, 1.33865662546e-10, -1.65439044196e-7, 1.81030980110e-10,
37 5.45753645958e5, -3.63192281933e7, 4.81463473761, 1.56633022620e5,
38 7.89977010972e-5, 1.39993881210e-2, -1.70656092212e-11, -4.55256623445e-5,
39 -2.29314170748e-14,8.31548197665e-12, 6.84673626259e-20,
40 -4.70845544152e-17, 5.21465091383e-16
41};
42
43static const double Dmeth[]=
44{ -1.78860165e-1, 4.83847500e-2, -1.84898700e-2 };
45
46static const double Fmeth[]=
47{ 4.77748580, 1.76065363, -5.67888940e-1, 1.32786231 };
48
49static const double Gmeth[]=
50{ 1.34740610e3, 1.35512060e2, -2.93910458e1, 2.12774600, 2.44656600e3 };
51
52double methane::C(int i, double rt, double rt2)
53{
54 switch (i) {
55 case 0:
56 return Ameth[0] * T + Ameth[1] * sqrt(T) + Ameth[2] + (Ameth[3] + Ameth[4] * rt) * rt;
57 case 1:
58 return Ameth[5] * T + Ameth[6] + rt * (Ameth[7] + Ameth[8] * rt);
59 case 2:
60 return Ameth[9] * T + Ameth[10] + Ameth[11] * rt;
61 case 3:
62 return Ameth[12];
63 case 4:
64 return rt*(Ameth[13] + Ameth[14]*rt);
65 case 5:
66 return Ameth[15]*rt;
67 case 6:
68 return rt*(Ameth[16] + Ameth[17]*rt);
69 case 7:
70 return Ameth[18]*rt2;
71 case 8:
72 return rt2*(Ameth[19] + Ameth[20]*rt);
73 case 9:
74 return rt2*(Ameth[21] + Ameth[22]*rt2);
75 case 10:
76 return rt2*(Ameth[23] + Ameth[24]*rt);
77 case 11:
78 return rt2*(Ameth[25] + Ameth[26]*rt2);
79 case 12:
80 return rt2*(Ameth[27] + Ameth[28]*rt);
81 case 13:
82 return rt2*(Ameth[29] + Ameth[30]*rt + Ameth[31]*rt2);
83 default:
84 return 0.0;
85 }
86}
87
88double methane::Cprime(int i, double rt, double rt2, double rt3)
89{
90 switch (i) {
91 case 0:
92 return Ameth[0] + 0.5*Ameth[1]/sqrt(T) - (Ameth[3] + 2.0*Ameth[4]*rt)*rt2;
93 case 1:
94 return Ameth[5] - rt2*(Ameth[7] + 2.0*Ameth[8]*rt);
95 case 2:
96 return Ameth[9] - Ameth[11]*rt2;
97 case 3:
98 return 0.0;
99 case 4:
100 return -rt2*(Ameth[13] + 2.0*Ameth[14]*rt);
101 case 5:
102 return -Ameth[15]*rt2;
103 case 6:
104 return -rt2*(Ameth[16] + 2.0*Ameth[17]*rt);
105 case 7:
106 return -2.0*Ameth[18]*rt3;
107 case 8:
108 return -rt3*(2.0*Ameth[19] + 3.0*Ameth[20]*rt);
109 case 9:
110 return -rt3*(2.0*Ameth[21] + 4.0*Ameth[22]*rt2);
111 case 10:
112 return -rt3*(2.0*Ameth[23] + 3.0*Ameth[24]*rt);
113 case 11:
114 return -rt3*(2.0*Ameth[25] + 4.0*Ameth[26]*rt2);
115 case 12:
116 return -rt3*(2.0*Ameth[27] + 3.0*Ameth[28]*rt);
117 case 13:
118 return -rt3*(2.0*Ameth[29] + 3.0*Ameth[30]*rt + 4.0*Ameth[31]*rt2);
119 default:
120 return 0.0;
121 }
122}
123
124double methane::W(int n, double egrho)
125{
126 return (n == 0 ? (1.0 - egrho)/(2.0*Gamma) :
127 (n*W(n-1, egrho) - 0.5*pow(Rho,2*n)*egrho)/Gamma);
128}
129
130double methane::H(int i, double egrho)
131{
132 return (i < 8 ? pow(Rho,i+2) : pow(Rho,2*i-13)*egrho);
133}
134
135double methane::I(int i, double egrho)
136{
137 return (i < 8 ? pow(Rho,i+1)/double(i+1) : W(i-8, egrho));
138}
139
141{
142 double rt = 1.0/T;
143 double rt2 = rt*rt;
144 double rt3 = rt*rt2;
145 double egrho = exp(-Gamma*Rho*Rho);
146 double t3 = pow(T,1.0/3.0);
147
148 double sum = 0.0;
149 for (int i=0; i<14; i++) {
150 sum += (C(i, rt, rt2) - T*Cprime(i, rt, rt2, rt3))*I(i, egrho);
151 }
152 sum += T*(Gmeth[0] + 0.75*Gmeth[1]*t3 + 0.6*Gmeth[2]*t3*t3 + 0.5*Gmeth[3]*T)
153 + Gmeth[4]*beta/(exp(beta*rt) - 1.0) + u0;
154 return sum + m_energy_offset;
155}
156
158{
159 double rt = 1.0/T;
160 double rt2 = rt*rt;
161 double rt3 = rt*rt2;
162 double egrho = exp(-Gamma*Rho*Rho);
163 double t3 = pow(T,1.0/3.0);
164 double sum = 0.0;
165 sum = s0 - R*log(Rho);
166 for (int i=0; i<14; i++) {
167 sum -= Cprime(i, rt, rt2, rt3)*I(i, egrho);
168 }
169 sum += Gmeth[0]*log(T) + 3.0*Gmeth[1]*t3 + 1.5*Gmeth[2]*t3*t3 + Gmeth[3]*T
170 + Gmeth[4]*(beta*rt + beta*rt/(exp(beta*rt) - 1.0)
171 - log(exp(beta*rt) - 1.0));
172 return sum + m_entropy_offset;
173}
174
175double methane::Pp()
176{
177 double rt = 1.0/T;
178 double rt2 = rt*rt;
179 double egrho = exp(-Gamma*Rho*Rho);
180
181 double P = Rho*R*T;
182 for (int i=0; i<14; i++) {
183 P += C(i, rt, rt2)*H(i, egrho);
184 }
185 return P;
186}
187
189{
190 double x = (1.0 - Tt/T)/(1.0 - Tt/Tc);
191 double result;
192 if ((T < Tmn) || (T > Tc)) {
193 throw CanteraError("methane::Psat",
194 "Temperature out of range. T = {}", T);
195 }
196 result = Fmeth[0]*x + Fmeth[1]*x*x + Fmeth[2]*x*x*x +
197 Fmeth[3]*x*pow(1-x, alpha);
198 return exp(result)*Pt;
199}
200
202{
203 double result;
204 double sum;
205 double w;
206 if ((T < Tmn) || (T > Tc)) {
207 throw CanteraError("methane::ldens",
208 "Temperature out of range. T = {}", T);
209 }
210 w = (Tc - T)/(Tc - Tt);
211 sum = Dmeth[0]*(1.0 - pow(w, 2.0/3.0)) + Dmeth[1]*(1.0 - pow(w, 4.0/3.0))
212 + Dmeth[2]*(1.0 - pow(w, 2));
213 result = pow(w,alpha1)*exp(sum);
214 result *= (Rot-Roc);
215 result += Roc;
216 return result;
217}
218
220{
221 return Tc;
222}
224{
225 return Pc;
226}
228{
229 return 1.0/Roc;
230}
232{
233 return Tmn;
234}
236{
237 return Tmx;
238}
240{
241 return M;
242}
243
244}
Base class for exceptions thrown by Cantera classes.
double x()
Vapor mass fraction.
Definition Sub.cpp:262
double P()
Pressure [Pa].
Definition Sub.cpp:35
double Tmax() override
Maximum temperature for which the equation of state is valid.
Definition Methane.cpp:235
double up() override
Internal energy of a single-phase state.
Definition Methane.cpp:140
double ldens() override
Liquid density. Equation D3 from Reynolds TPSI.
Definition Methane.cpp:201
double Tmin() override
Minimum temperature for which the equation of state is valid.
Definition Methane.cpp:231
double Tcrit() override
Critical temperature [K].
Definition Methane.cpp:219
double sp() override
Entropy of a single-phase state.
Definition Methane.cpp:157
double MolWt() override
Molecular weight [kg/kmol].
Definition Methane.cpp:239
double Vcrit() override
Critical specific volume [m^3/kg].
Definition Methane.cpp:227
double Pcrit() override
Critical pressure [Pa].
Definition Methane.cpp:223
double Psat() override
Saturation pressure. Equation S3 from Reynolds TPSI.
Definition Methane.cpp:188
Namespace for the Cantera kernel.
Definition AnyMap.cpp:595
Contains declarations for string manipulation functions within Cantera.