NitrogenFluidPropertiesTest.C File Reference

Go to the source code of this file.

Functions
	TEST_F (NitrogenFluidPropertiesTest, fluidName)
	Test that the fluid name is correctly returned.
	TEST_F (NitrogenFluidPropertiesTest, molarMass)
	Test that the molar mass is correctly returned.
	TEST_F (NitrogenFluidPropertiesTest, criticalProperties)
	Test that the critical properties are correctly returned.
	TEST_F (NitrogenFluidPropertiesTest, triplePointProperties)
	Test that the triple point properties are correctly returned.
	TEST_F (NitrogenFluidPropertiesTest, vapor)
	Verify calculation of vapor pressure, vapor density and saturated liquid density.
	TEST_F (NitrogenFluidPropertiesTest, henry)
	Verify that the coefficients for Henry's constant are correct using Guidelines on the Henry's constant and vapour liquid distribution constant for gases in H20 and D20 at high temperatures, IAPWS (2004).
	TEST_F (NitrogenFluidPropertiesTest, thermalConductivity)
	Verify calculation of thermal conductivity using data from Lemmon and Jacobsen, Viscosity and Thermal Conductivity Equations for Nitrogen, Oxygen, Argon, and Air, International Journal of Thermophysics, 25, 21–69 (2004)
	TEST_F (NitrogenFluidPropertiesTest, viscosity)
	Verify calculation of viscosity using data from Lemmon and Jacobsen, Viscosity and Thermal Conductivity Equations for Nitrogen, Oxygen, Argon, and Air, International Journal of Thermophysics, 25, 21–69 (2004)
	TEST_F (NitrogenFluidPropertiesTest, properties)
	Verify calculation of thermophysical properties of Nitrogen from the Span et al EOS using verification data provided in "A reference equation of state for the thermodynamic properties of nitrogen for temeperatures from 63.151 to 1000 K and pressures to 2200 MPa", Journal of Physical and Chemical Reference Data, 29, 1361–1433 (2000)
	TEST_F (NitrogenFluidPropertiesTest, derivatives)
	Verify calculation of the derivatives of all properties by comparing with finite differences.
	TEST_F (NitrogenFluidPropertiesTest, combined)
	Verify that the methods that return multiple properties in one call return identical values as the individual methods.

Function Documentation

TEST_F() [1/11]

TEST_F	(	NitrogenFluidPropertiesTest	,
		combined
	)

Verify that the methods that return multiple properties in one call return identical values as the individual methods.

Definition at line 222 of file NitrogenFluidPropertiesTest.C.

{
  const Real p = 1.0e6;
  const Real T = 300.0;
  const Real tol = REL_TOL_CONSISTENCY;
 
  // Single property methods
  Real rho, drho_dp, drho_dT;
  _fp->rho_from_p_T(p, T, rho, drho_dp, drho_dT);
  Real mu, dmu_dp, dmu_dT;
  _fp->mu_from_p_T(p, T, mu, dmu_dp, dmu_dT);
  Real e, de_dp, de_dT;
  _fp->e_from_p_T(p, T, e, de_dp, de_dT);
 
  // Combined property methods
  Real rho2, drho2_dp, drho2_dT, mu2, dmu2_dp, dmu2_dT, e2, de2_dp, de2_dT;
  _fp->rho_mu_from_p_T(p, T, rho2, mu2);
 
  ABS_TEST(rho, rho2, tol);
  ABS_TEST(mu, mu2, tol);
 
  _fp->rho_mu_from_p_T(p, T, rho2, drho2_dp, drho2_dT, mu2, dmu2_dp, dmu2_dT);
  ABS_TEST(rho, rho2, tol);
  ABS_TEST(drho_dp, drho2_dp, tol);
  ABS_TEST(drho_dT, drho2_dT, tol);
  ABS_TEST(mu, mu2, tol);
  ABS_TEST(dmu_dp, dmu2_dp, tol);
  ABS_TEST(dmu_dT, dmu2_dT, tol);
 
  _fp->rho_e_from_p_T(p, T, rho2, drho2_dp, drho2_dT, e2, de2_dp, de2_dT);
  ABS_TEST(rho, rho2, tol);
  ABS_TEST(drho_dp, drho2_dp, tol);
  ABS_TEST(drho_dT, drho2_dT, tol);
  ABS_TEST(e, e2, tol);
  ABS_TEST(de_dp, de2_dp, tol);
  ABS_TEST(de_dT, de2_dT, tol);
}

TEST_F() [2/11]

TEST_F	(	NitrogenFluidPropertiesTest	,
		criticalProperties
	)

Test that the critical properties are correctly returned.

Definition at line 29 of file NitrogenFluidPropertiesTest.C.

{
  ABS_TEST(_fp->criticalPressure(), 3.3958e6, REL_TOL_SAVED_VALUE);
  ABS_TEST(_fp->criticalTemperature(), 126.192, REL_TOL_SAVED_VALUE);
  ABS_TEST(_fp->criticalDensity(), 313.3, REL_TOL_SAVED_VALUE);
}

TEST_F() [3/11]

TEST_F	(	NitrogenFluidPropertiesTest	,
		derivatives
	)

Verify calculation of the derivatives of all properties by comparing with finite differences.

Definition at line 165 of file NitrogenFluidPropertiesTest.C.

{
  const Real tol = REL_TOL_DERIVATIVE;
 
  const Real p = 1.0e6;
  Real T = 350.0;
 
  DERIV_TEST(_fp->rho_from_p_T, p, T, tol);
  DERIV_TEST(_fp->mu_from_p_T, p, T, tol);
  DERIV_TEST(_fp->e_from_p_T, p, T, tol);
  DERIV_TEST(_fp->h_from_p_T, p, T, tol);
  DERIV_TEST(_fp->k_from_p_T, p, T, tol);
 
  // Viscosity from density and temperature
  T = 360.0;
  const Real drho = 1.0e-4;
  Real rho, drho_dp, drho_dT;
  _fp->rho_from_p_T(p, T, rho, drho_dp, drho_dT);
 
  Real dmu_drho_fd =
      (_fp->mu_from_rho_T(rho + drho, T) - _fp->mu_from_rho_T(rho - drho, T)) / (2.0 * drho);
  Real mu = 0.0, dmu_drho = 0.0, dmu_dT = 0.0;
  _fp->mu_from_rho_T(rho, T, drho_dT, mu, dmu_drho, dmu_dT);
 
  ABS_TEST(mu, _fp->mu_from_rho_T(rho, T), REL_TOL_CONSISTENCY);
  REL_TEST(dmu_drho, dmu_drho_fd, tol);
 
  // To properly test derivative wrt temperature, use p and T and calculate density,
  // so that the change in density wrt temperature is included
  const Real dp = 1.0e1;
  const Real dT = 1.0e-4;
  _fp->rho_from_p_T(p, T, rho, drho_dp, drho_dT);
  _fp->mu_from_rho_T(rho, T, drho_dT, mu, dmu_drho, dmu_dT);
 
  Real dmu_dT_fd = (_fp->mu_from_rho_T(_fp->rho_from_p_T(p, T + dT), T + dT) -
                    _fp->mu_from_rho_T(_fp->rho_from_p_T(p, T - dT), T - dT)) /
                   (2.0 * dT);
 
  REL_TEST(dmu_dT, dmu_dT_fd, tol);
 
  Real dmu_dp_fd = (_fp->mu_from_p_T(p + dp, T) - _fp->mu_from_p_T(p - dp, T)) / (2.0 * dp);
  Real dmu_dp = 0.0;
  _fp->mu_from_p_T(p, T, mu, dmu_dp, dmu_dT);
 
  ABS_TEST(mu, _fp->mu_from_p_T(p, T), REL_TOL_CONSISTENCY);
  REL_TEST(dmu_dp, dmu_dp_fd, tol);
 
  _fp->mu_from_p_T(p, T, mu, dmu_dp, dmu_dT);
  dmu_dT_fd = (_fp->mu_from_p_T(p, T + dT) - _fp->mu_from_p_T(p, T - dT)) / (2.0 * dT);
 
  REL_TEST(dmu_dT, dmu_dT_fd, tol);
}

TEST_F() [4/11]

TEST_F	(	NitrogenFluidPropertiesTest	,
		fluidName
	)

Test that the fluid name is correctly returned.

Definition at line 16 of file NitrogenFluidPropertiesTest.C.

{ EXPECT_EQ(_fp->fluidName(), "nitrogen"); }

TEST_F() [5/11]

TEST_F	(	NitrogenFluidPropertiesTest	,
		henry
	)

Verify that the coefficients for Henry's constant are correct using Guidelines on the Henry's constant and vapour liquid distribution constant for gases in H20 and D20 at high temperatures, IAPWS (2004).

Definition at line 74 of file NitrogenFluidPropertiesTest.C.

{
  const Real tol = REL_TOL_EXTERNAL_VALUE;
  const std::vector<Real> hc = _fp->henryCoefficients();
 
  REL_TEST(hc[0], -9.67578, tol);
  REL_TEST(hc[1], 4.72162, tol);
  REL_TEST(hc[2], 11.70585, tol);
}

TEST_F() [6/11]

TEST_F	(	NitrogenFluidPropertiesTest	,
		molarMass
	)

Test that the molar mass is correctly returned.

Definition at line 21 of file NitrogenFluidPropertiesTest.C.

{
  ABS_TEST(_fp->molarMass(), 28.01348e-3, REL_TOL_SAVED_VALUE);
}

TEST_F() [7/11]

TEST_F	(	NitrogenFluidPropertiesTest	,
		properties
	)

Verify calculation of thermophysical properties of Nitrogen from the Span et al EOS using verification data provided in "A reference equation of state for the thermodynamic properties of nitrogen for temeperatures from 63.151 to 1000 K and pressures to 2200 MPa", Journal of Physical and Chemical Reference Data, 29, 1361–1433 (2000)

Definition at line 124 of file NitrogenFluidPropertiesTest.C.

{
  // Pressure = 1 MPa, temperature = 280 K
  Real p = 1.0e6;
  Real T = 280.0;
 
  const Real tol = REL_TOL_EXTERNAL_VALUE;
 
  REL_TEST(_fp->rho_from_p_T(p, T), 0.43104 * 1000.0 * _fp->molarMass(), tol);
  REL_TEST(_fp->h_from_p_T(p, T), 8070.2 / _fp->molarMass(), tol);
  REL_TEST(_fp->e_from_p_T(p, T), 5750.3 / _fp->molarMass(), tol);
  REL_TEST(_fp->s_from_p_T(p, T), 170.41 / _fp->molarMass(), tol);
  REL_TEST(_fp->cp_from_p_T(p, T), 29.66 / _fp->molarMass(), tol);
  REL_TEST(_fp->cv_from_p_T(p, T), 20.89 / _fp->molarMass(), tol);
  REL_TEST(_fp->c_from_p_T(p, T), 342.4, tol);
 
  // Pressure = 1 MPa, temperature = 500 K
  T = 500.0;
  REL_TEST(_fp->rho_from_p_T(p, T), 0.23958 * 1000.0 * _fp->molarMass(), tol);
  REL_TEST(_fp->e_from_p_T(p, T), 10395.0 / _fp->molarMass(), tol);
  REL_TEST(_fp->h_from_p_T(p, T), 14569.0 / _fp->molarMass(), tol);
  REL_TEST(_fp->s_from_p_T(p, T), 187.54 / _fp->molarMass(), tol);
  REL_TEST(_fp->cp_from_p_T(p, T), 29.72 / _fp->molarMass(), tol);
  REL_TEST(_fp->cv_from_p_T(p, T), 21.29 / _fp->molarMass(), tol);
  REL_TEST(_fp->c_from_p_T(p, T), 457.0, tol);
 
  // Pressure = 10 MPa, temperature = 500 K
  p = 10.0e6;
  REL_TEST(_fp->rho_from_p_T(p, T), 2.3024 * 1000.0 * _fp->molarMass(), tol);
  REL_TEST(_fp->e_from_p_T(p, T), 10154.0 / _fp->molarMass(), tol);
  REL_TEST(_fp->h_from_p_T(p, T), 14497.0 / _fp->molarMass(), tol);
  REL_TEST(_fp->s_from_p_T(p, T), 167.93 / _fp->molarMass(), tol);
  REL_TEST(_fp->cp_from_p_T(p, T), 30.82 / _fp->molarMass(), tol);
  REL_TEST(_fp->cv_from_p_T(p, T), 21.49 / _fp->molarMass(), tol);
  REL_TEST(_fp->c_from_p_T(p, T), 483.1, tol);
}

TEST_F() [8/11]

TEST_F	(	NitrogenFluidPropertiesTest	,
		thermalConductivity
	)

Verify calculation of thermal conductivity using data from Lemmon and Jacobsen, Viscosity and Thermal Conductivity Equations for Nitrogen, Oxygen, Argon, and Air, International Journal of Thermophysics, 25, 21–69 (2004)

Definition at line 89 of file NitrogenFluidPropertiesTest.C.

{
  const Real tol = REL_TOL_EXTERNAL_VALUE;
 
  REL_TEST(_fp->k_from_rho_T(0.0, 300.0), 25.9361e-3, tol);
  REL_TEST(_fp->k_from_rho_T(5.0 * 1000.0 * _fp->molarMass(), 300.0), 32.7694e-3, tol);
 
  const Real p = _fp->p_from_rho_T(5.0 * 1000.0 * _fp->molarMass(), 300.0);
  REL_TEST(_fp->k_from_p_T(p, 300.0), 32.7694e-3, tol);
}

TEST_F() [9/11]

TEST_F	(	NitrogenFluidPropertiesTest	,
		triplePointProperties
	)

Test that the triple point properties are correctly returned.

Definition at line 39 of file NitrogenFluidPropertiesTest.C.

{
  ABS_TEST(_fp->triplePointPressure(), 12.523e3, REL_TOL_SAVED_VALUE);
  ABS_TEST(_fp->triplePointTemperature(), 63.151, REL_TOL_SAVED_VALUE);
}

TEST_F() [10/11]

TEST_F	(	NitrogenFluidPropertiesTest	,
		vapor
	)

Verify calculation of vapor pressure, vapor density and saturated liquid density.

Definition at line 49 of file NitrogenFluidPropertiesTest.C.

{
  const Real tol = REL_TOL_EXTERNAL_VALUE;
 
  // Vapor pressure
  REL_TEST(_fp->vaporPressure(80.0), 0.13687e6, tol);
  REL_TEST(_fp->vaporPressure(100.0), 0.77827e6, tol);
  REL_TEST(_fp->vaporPressure(120.0), 2.51058e6, tol);
  //
  // Saturated vapor density
  REL_TEST(_fp->saturatedVaporDensity(80.0), 0.21737 * 1000.0 * _fp->molarMass(), tol);
  REL_TEST(_fp->saturatedVaporDensity(100.0), 1.1409 * 1000.0 * _fp->molarMass(), tol);
  REL_TEST(_fp->saturatedVaporDensity(120.0), 4.4653 * 1000.0 * _fp->molarMass(), tol);
 
  // Saturated liquid density
  REL_TEST(_fp->saturatedLiquidDensity(80.0), 28.341 * 1000.0 * _fp->molarMass(), tol);
  REL_TEST(_fp->saturatedLiquidDensity(100.0), 24.608 * 1000.0 * _fp->molarMass(), tol);
  REL_TEST(_fp->saturatedLiquidDensity(120.0), 18.682 * 1000.0 * _fp->molarMass(), tol);
}

TEST_F() [11/11]

TEST_F	(	NitrogenFluidPropertiesTest	,
		viscosity
	)

Verify calculation of viscosity using data from Lemmon and Jacobsen, Viscosity and Thermal Conductivity Equations for Nitrogen, Oxygen, Argon, and Air, International Journal of Thermophysics, 25, 21–69 (2004)

Definition at line 105 of file NitrogenFluidPropertiesTest.C.

{
  const Real tol = REL_TOL_EXTERNAL_VALUE;
 
  REL_TEST(_fp->mu_from_rho_T(0.0, 100.0), 6.90349e-6, tol);
  REL_TEST(_fp->mu_from_rho_T(25.0 * 1000.0 * _fp->molarMass(), 100.0), 79.7418e-6, tol);
  REL_TEST(_fp->mu_from_rho_T(10.0 * 1000.0 * _fp->molarMass(), 200.0), 21.081e-6, tol);
 
  const Real p = _fp->p_from_rho_T(5.0 * 1000.0 * _fp->molarMass(), 300.0);
  REL_TEST(_fp->mu_from_p_T(p, 300.0), 20.7430e-6, tol);
}