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HydrogenFluidPropertiesTest.C
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1//* This file is part of the MOOSE framework
2//* https://mooseframework.inl.gov
3//*
4//* All rights reserved, see COPYRIGHT for full restrictions
5//* https://github.com/idaholab/moose/blob/master/COPYRIGHT
6//*
7//* Licensed under LGPL 2.1, please see LICENSE for details
8//* https://www.gnu.org/licenses/lgpl-2.1.html
9
10#include "HydrogenFluidPropertiesTest.h"
11#include "SinglePhaseFluidPropertiesTestUtils.h"
12
16TEST_F(HydrogenFluidPropertiesTest, fluidName) { EXPECT_EQ(_fp->fluidName(), "hydrogen"); }
17
21TEST_F(HydrogenFluidPropertiesTest, molarMass)
22{
23 ABS_TEST(_fp->molarMass(), 2.01588e-3, REL_TOL_SAVED_VALUE);
24}
25
29TEST_F(HydrogenFluidPropertiesTest, criticalProperties)
30{
31 ABS_TEST(_fp->criticalPressure(), 1.315e6, REL_TOL_SAVED_VALUE);
32 ABS_TEST(_fp->criticalTemperature(), 33.19, REL_TOL_SAVED_VALUE);
33 ABS_TEST(_fp->criticalDensity(), 31.26226704, REL_TOL_SAVED_VALUE);
34}
35
39TEST_F(HydrogenFluidPropertiesTest, triplePointProperties)
40{
41 ABS_TEST(_fp->triplePointPressure(), 7.7e3, REL_TOL_SAVED_VALUE);
42 ABS_TEST(_fp->triplePointTemperature(), 13.952, REL_TOL_SAVED_VALUE);
43}
44
49TEST_F(HydrogenFluidPropertiesTest, vapor)
50{
51 const Real tol = 10.0 * REL_TOL_EXTERNAL_VALUE;
52
53 // Vapor pressure
54 REL_TEST(_fp->vaporPressure(14.0), 7.541e3, tol);
55 REL_TEST(_fp->vaporPressure(30.0), 0.80432e6, tol);
56}
57
63TEST_F(HydrogenFluidPropertiesTest, henry)
64{
65 const Real tol = REL_TOL_EXTERNAL_VALUE;
66 const std::vector<Real> hc = _fp->henryCoefficients();
67
68 REL_TEST(hc[0], -4.73284, tol);
69 REL_TEST(hc[1], 6.08954, tol);
70 REL_TEST(hc[2], 6.06066, tol);
71}
72
79TEST_F(HydrogenFluidPropertiesTest, thermalConductivity)
80{
81 const Real tol = REL_TOL_EXTERNAL_VALUE;
82
83 REL_TEST(_fp->k_from_rho_T(0.80844, 298.15), 186.97e-3, tol);
84 REL_TEST(_fp->k_from_rho_T(30.0, 35.0), 71.854e-3, tol);
85 REL_TEST(_fp->k_from_rho_T(15.879, 400.0), 248.6e-3, tol);
86
87 REL_TEST(_fp->k_from_p_T(30.0e6, 400.0), 248.6e-3, tol);
88}
89
96TEST_F(HydrogenFluidPropertiesTest, viscosity)
97{
98 const Real tol = 10.0 * REL_TOL_EXTERNAL_VALUE;
99
100 REL_TEST(_fp->mu_from_rho_T(0.0, 298.15), 8.8997e-6, tol);
101 REL_TEST(_fp->mu_from_rho_T(0.68911, 350.0), 9.9645e-6, tol);
102 REL_TEST(_fp->mu_from_rho_T(6.5764, 350.0), 1.0147e-5, tol);
103
104 REL_TEST(_fp->mu_from_p_T(1.0e6, 350.0), 9.9645e-6, tol);
105 REL_TEST(_fp->mu_from_p_T(10.0e6, 350.0), 1.0147e-5, tol);
106}
107
112TEST_F(HydrogenFluidPropertiesTest, properties)
113{
114 // Pressure = 1 MPa, temperature = 280 K
115 Real p = 1.0e6;
116 Real T = 280.0;
117
118 const Real tol = REL_TOL_EXTERNAL_VALUE;
119
120 REL_TEST(_fp->rho_from_p_T(p, T), 0.86069, tol);
121 REL_TEST(_fp->h_from_p_T(p, T), 3676.1e3, tol);
122 REL_TEST(_fp->e_from_p_T(p, T), 2514.2e3, tol);
123 REL_TEST(_fp->s_from_p_T(p, T), 43.025e3, tol);
124 REL_TEST(_fp->cp_from_p_T(p, T), 14.26e3, tol);
125 REL_TEST(_fp->cv_from_p_T(p, T), 10.112e3, tol);
126 REL_TEST(_fp->c_from_p_T(p, T), 1283.9, tol);
127
128 // Pressure = 1 MPa, temperature = 500 K
129 T = 500.0;
130 REL_TEST(_fp->rho_from_p_T(p, T), 0.48302, tol);
131 REL_TEST(_fp->h_from_p_T(p, T), 6856.5e3, tol);
132 REL_TEST(_fp->e_from_p_T(p, T), 4786.2e3, tol);
133 REL_TEST(_fp->s_from_p_T(p, T), 51.401e3, tol);
134 REL_TEST(_fp->cp_from_p_T(p, T), 14.52e3, tol);
135 REL_TEST(_fp->cv_from_p_T(p, T), 10.392e3, tol);
136 REL_TEST(_fp->c_from_p_T(p, T), 1704.1, tol);
137
138 // Pressure = 10 MPa, temperature = 500 K
139 p = 10.0e6;
140 REL_TEST(_fp->rho_from_p_T(p, T), 4.6658, tol);
141 REL_TEST(_fp->h_from_p_T(p, T), 6923.4e3, tol);
142 REL_TEST(_fp->e_from_p_T(p, T), 4780.1e3, tol);
143 REL_TEST(_fp->s_from_p_T(p, T), 41.892e3, tol);
144 REL_TEST(_fp->cp_from_p_T(p, T), 14.584e3, tol);
145 REL_TEST(_fp->cv_from_p_T(p, T), 10.436e3, tol);
146 REL_TEST(_fp->c_from_p_T(p, T), 1764.3, tol);
147}
148
153TEST_F(HydrogenFluidPropertiesTest, derivatives)
154{
155 const Real tol = REL_TOL_DERIVATIVE;
156
157 const Real p = 1.0e6;
158 Real T = 350.0;
159
160 DERIV_TEST(_fp->rho_from_p_T, p, T, tol);
161 DERIV_TEST(_fp->mu_from_p_T, p, T, tol);
162 DERIV_TEST(_fp->e_from_p_T, p, T, tol);
163 DERIV_TEST(_fp->h_from_p_T, p, T, tol);
164 DERIV_TEST(_fp->k_from_p_T, p, T, tol);
165
166 // Viscosity from density and temperature
167 T = 360.0;
168 const Real drho = 1.0e-4;
169 Real rho, drho_dp, drho_dT;
170 _fp->rho_from_p_T(p, T, rho, drho_dp, drho_dT);
171
172 Real dmu_drho_fd =
173 (_fp->mu_from_rho_T(rho + drho, T) - _fp->mu_from_rho_T(rho - drho, T)) / (2.0 * drho);
174 Real mu = 0.0, dmu_drho = 0.0, dmu_dT = 0.0;
175 _fp->mu_from_rho_T(rho, T, drho_dT, mu, dmu_drho, dmu_dT);
176
177 ABS_TEST(mu, _fp->mu_from_rho_T(rho, T), REL_TOL_CONSISTENCY);
178 REL_TEST(dmu_drho, dmu_drho_fd, tol);
179
180 // To properly test derivative wrt temperature, use p and T and calculate density,
181 // so that the change in density wrt temperature is included
182 const Real dp = 1.0e1;
183 const Real dT = 1.0e-4;
184 _fp->rho_from_p_T(p, T, rho, drho_dp, drho_dT);
185 _fp->mu_from_rho_T(rho, T, drho_dT, mu, dmu_drho, dmu_dT);
186
187 Real dmu_dT_fd = (_fp->mu_from_rho_T(_fp->rho_from_p_T(p, T + dT), T + dT) -
188 _fp->mu_from_rho_T(_fp->rho_from_p_T(p, T - dT), T - dT)) /
189 (2.0 * dT);
190
191 REL_TEST(dmu_dT, dmu_dT_fd, tol);
192
193 Real dmu_dp_fd = (_fp->mu_from_p_T(p + dp, T) - _fp->mu_from_p_T(p - dp, T)) / (2.0 * dp);
194 Real dmu_dp = 0.0;
195 _fp->mu_from_p_T(p, T, mu, dmu_dp, dmu_dT);
196
197 ABS_TEST(mu, _fp->mu_from_p_T(p, T), REL_TOL_CONSISTENCY);
198 REL_TEST(dmu_dp, dmu_dp_fd, tol);
199
200 _fp->mu_from_p_T(p, T, mu, dmu_dp, dmu_dT);
201 dmu_dT_fd = (_fp->mu_from_p_T(p, T + dT) - _fp->mu_from_p_T(p, T - dT)) / (2.0 * dT);
202
203 REL_TEST(dmu_dT, dmu_dT_fd, tol);
204}
205
210TEST_F(HydrogenFluidPropertiesTest, combined)
211{
212 const Real p = 1.0e6;
213 const Real T = 300.0;
214 const Real tol = REL_TOL_CONSISTENCY;
215
216 // Single property methods
217 Real rho, drho_dp, drho_dT;
218 _fp->rho_from_p_T(p, T, rho, drho_dp, drho_dT);
219 Real mu, dmu_dp, dmu_dT;
220 _fp->mu_from_p_T(p, T, mu, dmu_dp, dmu_dT);
221 Real e, de_dp, de_dT;
222 _fp->e_from_p_T(p, T, e, de_dp, de_dT);
223
224 // Combined property methods
225 Real rho2, drho2_dp, drho2_dT, mu2, dmu2_dp, dmu2_dT, e2, de2_dp, de2_dT;
226 _fp->rho_mu_from_p_T(p, T, rho2, mu2);
227
228 ABS_TEST(rho, rho2, tol);
229 ABS_TEST(mu, mu2, tol);
230
231 _fp->rho_mu_from_p_T(p, T, rho2, drho2_dp, drho2_dT, mu2, dmu2_dp, dmu2_dT);
232 ABS_TEST(rho, rho2, tol);
233 ABS_TEST(drho_dp, drho2_dp, tol);
234 ABS_TEST(drho_dT, drho2_dT, tol);
235 ABS_TEST(mu, mu2, tol);
236 ABS_TEST(dmu_dp, dmu2_dp, tol);
237 ABS_TEST(dmu_dT, dmu2_dT, tol);
238
239 _fp->rho_e_from_p_T(p, T, rho2, drho2_dp, drho2_dT, e2, de2_dp, de2_dT);
240 ABS_TEST(rho, rho2, tol);
241 ABS_TEST(drho_dp, drho2_dp, tol);
242 ABS_TEST(drho_dT, drho2_dT, tol);
243 ABS_TEST(e, e2, tol);
244 ABS_TEST(de_dp, de2_dp, tol);
245 ABS_TEST(de_dT, de2_dT, tol);
246}
tol
const double tol
Definition EquilibriumConstantFitTest.C:16
mu
const double mu
Definition GasLiquidMassTransferTest.C:22
p
const Real p
Definition GasLiquidMassTransferTest.C:18
rho
const double rho
Definition GasLiquidMassTransferTest.C:27
T
const double T
Definition GasLiquidMassTransferTest.C:19
TEST_F
TEST_F(HydrogenFluidPropertiesTest, fluidName)
Test that the fluid name is correctly returned.
Definition HydrogenFluidPropertiesTest.C:16
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