www.mooseframework.org
Public Member Functions | Protected Types | Protected Member Functions | Protected Attributes | List of all members
NaNInterfaceTestFluidProperties Class Reference

Fluid properties for testing NaNInterface. More...

#include <NaNInterfaceTestFluidProperties.h>

Inheritance diagram for NaNInterfaceTestFluidProperties:
[legend]

Public Member Functions

 NaNInterfaceTestFluidProperties (const InputParameters &parameters)
 
virtual Real p_from_v_e (Real v, Real e) const override
 
virtual void p_from_v_e (Real v, Real e, Real &p, Real &dp_dv, Real &dp_de) const override
 
virtual Real rho (Real p, Real T) const
 Density from pressure and temperature. More...
 
virtual std::string fluidName () const
 Fluid name. More...
 
e e e e s T T T T T rho v v T virtual e Real s (Real pressure, Real temperature) const
 
virtual void mu_from_rho_T (Real density, Real temperature, Real ddensity_dT, Real &mu, Real &dmu_drho, Real &dmu_dT) const
 Dynamic viscosity and its derivatives wrt density and temperature TODO: this shouldn't need 3 input args - AD will assume/call the 2-input version. More...
 
virtual Real beta_from_p_T (Real, Real) const
 
virtual void beta_from_p_T (Real, Real, Real &, Real &, Real &) const
 
virtual void rho_dpT (Real pressure, Real temperature, Real &rho, Real &drho_dp, Real &drho_dT) const
 Density and its derivatives from pressure and temperature. More...
 
virtual Real v_from_p_T (Real p, Real T) const
 Specific volume from pressure and temperature. More...
 
virtual void v_from_p_T (Real p, Real T, Real &v, Real &dv_dp, Real &dv_dT) const
 Specific volume and its derivatives from pressure and temperature. More...
 
virtual Real e_spndl_from_v (Real v) const
 Specific internal energy from temperature and specific volume. More...
 
virtual void v_e_spndl_from_T (Real T, Real &v, Real &e) const
 Specific internal energy from temperature and specific volume. More...
 
virtual Real h (Real p, Real T) const
 Specific enthalpy from pressure and temperature. More...
 
virtual void h_dpT (Real pressure, Real temperature, Real &h, Real &dh_dp, Real &dh_dT) const
 Specific enthalpy and its derivatives from pressure and temperature. More...
 
virtual Real e_from_p_T (Real p, Real T) const
 Internal energy from pressure and temperature. More...
 
virtual void e_from_p_T (Real p, Real T, Real &e, Real &de_dp, Real &de_dT) const
 Internal energy and its derivatives from pressure and temperature. More...
 
virtual Real e (Real pressure, Real temperature) const
 
virtual void e_dpT (Real pressure, Real temperature, Real &e, Real &de_dp, Real &de_dT) const
 
virtual Real beta (Real pressure, Real temperature) const
 
virtual Real T_from_p_h (Real pressure, Real enthalpy) const
 Temperature from pressure and specific enthalpy. More...
 
virtual Real molarMass () const
 Molar mass [kg/mol]. More...
 
virtual Real criticalPressure () const
 Critical pressure. More...
 
virtual Real criticalTemperature () const
 Critical temperature. More...
 
virtual Real criticalDensity () const
 Critical density. More...
 
virtual Real criticalInternalEnergy () const
 Critical specific internal energy. More...
 
virtual Real triplePointPressure () const
 Triple point pressure. More...
 
virtual Real triplePointTemperature () const
 Triple point temperature. More...
 
virtual void rho_e_from_p_T (Real pressure, Real temperature, Real &rho, Real &drho_dp, Real &drho_dT, Real &e, Real &de_dp, Real &de_dT) const
 Density and internal energy and their derivatives wrt pressure and temperature. More...
 
virtual void rho_e_dpT (Real pressure, Real temperature, Real &rho, Real &drho_dp, Real &drho_dT, Real &e, Real &de_dp, Real &de_dT) const
 
virtual Real c (Real pressure, Real temperature) const
 
virtual Real gamma_from_p_T (Real pressure, Real temperature) const
 Adiabatic index - ratio of specific heats. More...
 
virtual Real mu (Real pressure, Real temperature) const
 Dynamic viscosity. More...
 
virtual void mu_dpT (Real pressure, Real temperature, Real &mu, Real &dmu_dp, Real &dmu_dT) const
 Dynamic viscosity and its derivatives wrt pressure and temperature. More...
 
virtual void mu_drhoT_from_rho_T (Real density, Real temperature, Real ddensity_dT, Real &mu, Real &dmu_drho, Real &dmu_dT) const
 
virtual void rho_mu (Real pressure, Real temperature, Real &rho, Real &mu) const
 Density and viscosity. More...
 
virtual void rho_mu_from_p_T (Real pressure, Real temperature, Real &rho, Real &mu) const
 
virtual void rho_mu_from_p_T (Real pressure, Real temperature, Real &rho, Real &drho_dp, Real &drho_dT, Real &mu, Real &dmu_dp, Real &dmu_dT) const
 Density and viscosity and their derivatives wrt pressure and temperature. More...
 
virtual void rho_mu_dpT (Real pressure, Real temperature, Real &rho, Real &drho_dp, Real &drho_dT, Real &mu, Real &dmu_dp, Real &dmu_dT) const
 
virtual Real k (Real pressure, Real temperature) const
 Thermal conductivity. More...
 
virtual void k_dpT (Real pressure, Real temperature, Real &k, Real &dk_dp, Real &dk_dT) const
 Thermal conductivity and its derivatives wrt pressure and temperature. More...
 
virtual Real henryConstant (Real temperature) const
 Henry's law constant for dissolution in water. More...
 
virtual void henryConstant (Real temperature, Real &Kh, Real &dKh_dT) const
 Henry's law constant for dissolution in water and derivative wrt temperature. More...
 
virtual void henryConstant_dT (Real temperature, Real &Kh, Real &dKh_dT) const
 
virtual Real vaporPressure (Real temperature) const
 Vapor pressure. More...
 
virtual void vaporPressure (Real temperature, Real &psat, Real &dpsat_dT) const
 Vapor pressure. More...
 
virtual void vaporPressure_dT (Real temperature, Real &psat, Real &dpsat_dT) const
 
virtual void execute () final
 
virtual void initialize () final
 
virtual void finalize () final
 
virtual void threadJoin (const UserObject &) final
 
virtual void subdomainSetup () final
 

Protected Types

enum  NaNMessage { NAN_MESSAGE_NONE = 0, NAN_MESSAGE_WARNING = 1, NAN_MESSAGE_ERROR = 2 }
 

Protected Member Functions

virtual Real henryConstantIAPWS (Real temperature, Real A, Real B, Real C) const
 IAPWS formulation of Henry's law constant for dissolution in water From Guidelines on the Henry's constant and vapour liquid distribution constant for gases in H20 and D20 at high temperatures, IAPWS (2004) More...
 
virtual void henryConstantIAPWS (Real temperature, Real &Kh, Real &dKh_dT, Real A, Real B, Real C) const
 
virtual void henryConstantIAPWS_dT (Real temperature, Real &Kh, Real &dKh_dT, Real A, Real B, Real C) const
 
Real getNaN () const
 Produces errors, warnings, or just quiet NaNs. More...
 
template<typename... Args>
Real getNaN (Args &&... args) const
 

Protected Attributes

const Real _R
 Universal gas constant (J/mol/K) More...
 
const Real _T_c2k
 Conversion of temperature from Celsius to Kelvin. More...
 
const MooseObject * _moose_object
 
enum NaNMessage _emit_on_nan
 Raise mooseWarning or mooseError? More...
 
 propfunc (p, v, e) propfunc(T
 Compute a fluid property given for the state defined by two given properties. More...
 
e propfunc (c, v, e) propfunc(cp
 
e e propfunc (cv, v, e) propfunc(mu
 
e e e propfunc (k, v, e) propfunc(s
 
e e e e propfunc (s, h, p) propfunc(rho
 
e e e e s propfunc (e, v, h) propfunc(s
 
e e e e s T propfunc (pp_sat, p, T) propfunc(mu
 
e e e e s T T propfunc (k, rho, T) propfunc(c
 
e e e e s T T T propfunc (cp, p, T) propfunc(cv
 
e e e e s T T T T propfunc (mu, p, T) propfunc(k
 
e e e e s T T T T T propfunc (rho, p, T) propfunc(e
 
e e e e s T T T T T rho propfunc (e, T, v) propfunc(p
 
e e e e s T T T T T rho v propfunc (h, T, v) propfunc(s
 
e e e e s T T T T T rho v v propfunc (cv, T, v) propfunc(h
 
e e e e s T T T T T rho v v T propfunc (p, h, s) propfunc(g
 
 v
 
e v
 
e e v
 
e e e v
 
e e e e s T T T T T rho v v T v
 
e e e e p
 
e e e e s p
 
e e e e s T T p
 
e e e e s T T T p
 
e e e e s T T T T p
 
e e e e s T T T T T p
 
e e e e s T T T T T rho v v p
 
e e e e s T rho
 
e e e e s T T T T T rho T
 
e e e e s T T T T T rho v T
 

Detailed Description

Fluid properties for testing NaNInterface.

Definition at line 24 of file NaNInterfaceTestFluidProperties.h.

Member Enumeration Documentation

◆ NaNMessage

enum NaNInterface::NaNMessage
protectedinherited
Enumerator
NAN_MESSAGE_NONE 
NAN_MESSAGE_WARNING 
NAN_MESSAGE_ERROR 

Definition at line 34 of file NaNInterface.h.

Constructor & Destructor Documentation

◆ NaNInterfaceTestFluidProperties()

NaNInterfaceTestFluidProperties::NaNInterfaceTestFluidProperties ( const InputParameters &  parameters)

Definition at line 26 of file NaNInterfaceTestFluidProperties.C.

27  : SinglePhaseFluidProperties(parameters), NaNInterface(this)
28 {
29 }
NaNInterface(const MooseObject *moose_object)
Definition: NaNInterface.C:33
SinglePhaseFluidProperties(const InputParameters &parameters)

Member Function Documentation

◆ beta()

Real SinglePhaseFluidProperties::beta ( Real  pressure,
Real  temperature 
) const
virtualinherited

◆ beta_from_p_T() [1/2]

Real SinglePhaseFluidProperties::beta_from_p_T ( Real  p,
Real  T 
) const
virtualinherited

Reimplemented in SimpleFluidProperties.

Definition at line 86 of file SinglePhaseFluidProperties.C.

Referenced by SinglePhaseFluidProperties::beta().

87 {
88  // The volumetric thermal expansion coefficient is defined as
89  // 1/v dv/dT)_p
90  // It is the fractional change rate of volume with respect to temperature change
91  // at constant pressure. Here it is coded as
92  // - 1/rho drho/dT)_p
93  // using chain rule with v = v(rho)
94 
95  Real rho, drho_dp, drho_dT;
96  rho_from_p_T(p, T, rho, drho_dp, drho_dT);
97  return -drho_dT / rho;
98 }

◆ beta_from_p_T() [2/2]

void SinglePhaseFluidProperties::beta_from_p_T ( Real  ,
Real  ,
Real &  ,
Real &  ,
Real &   
) const
virtualinherited

Reimplemented in SimpleFluidProperties.

Definition at line 80 of file SinglePhaseFluidProperties.C.

81 {
82  mooseError(name(), ": ", __PRETTY_FUNCTION__, " is not implemented.");
83 }
const std::string name
Definition: Setup.h:22

◆ c()

Real SinglePhaseFluidProperties::c ( Real  pressure,
Real  temperature 
) const
virtualinherited

Definition at line 337 of file SinglePhaseFluidProperties.C.

Referenced by IdealGasFluidProperties::c_from_v_e(), StiffenedGasFluidProperties::c_from_v_e(), Water97FluidProperties::densityRegion3(), Water97FluidProperties::subregionVolume(), and Water97FluidProperties::vaporPressure().

338 {
339  mooseDeprecated(name(), ": c() is deprecated. Use c_from_p_T() instead");
340 
341  return c_from_p_T(p, T);
342 }
const std::string name
Definition: Setup.h:22

◆ criticalDensity()

Real SinglePhaseFluidProperties::criticalDensity ( ) const
virtualinherited

◆ criticalInternalEnergy()

Real SinglePhaseFluidProperties::criticalInternalEnergy ( ) const
virtualinherited

Critical specific internal energy.

Returns
specific internal energy (J/kg)

Reimplemented in StiffenedGasFluidProperties.

Definition at line 131 of file SinglePhaseFluidProperties.C.

Referenced by IdealRealGasMixtureFluidProperties::p_T_from_v_e().

132 {
133  mooseError(name(), ": criticalInternalEnergy() is not implemented");
134 }
const std::string name
Definition: Setup.h:22

◆ criticalPressure()

Real SinglePhaseFluidProperties::criticalPressure ( ) const
virtualinherited

Critical pressure.

Returns
critical pressure (Pa)

Reimplemented in HydrogenFluidProperties, CO2FluidProperties, NitrogenFluidProperties, MethaneFluidProperties, NaClFluidProperties, and Water97FluidProperties.

Definition at line 113 of file SinglePhaseFluidProperties.C.

114 {
115  mooseError(name(), ": criticalPressure() is not implemented");
116 }
const std::string name
Definition: Setup.h:22

◆ criticalTemperature()

Real SinglePhaseFluidProperties::criticalTemperature ( ) const
virtualinherited

◆ e()

Real SinglePhaseFluidProperties::e ( Real  pressure,
Real  temperature 
) const
virtualinherited

Definition at line 292 of file SinglePhaseFluidProperties.C.

Referenced by Water97FluidProperties::b2bc(), IdealGasFluidProperties::c_from_v_e(), StiffenedGasFluidProperties::c_from_v_e(), NaClFluidProperties::cp_from_p_T(), IdealGasFluidProperties::cp_from_v_e(), StiffenedGasFluidProperties::cp_from_v_e(), Water97FluidProperties::densityRegion3(), SinglePhaseFluidProperties::e_dpT(), StiffenedGasFluidProperties::e_from_p_rho(), IdealGasFluidProperties::e_from_p_rho(), HelmholtzFluidProperties::e_from_p_T(), IdealGasFluidPropertiesPT::e_from_p_T(), Water97FluidProperties::e_from_p_T(), NaClFluidProperties::e_from_p_T(), IdealGasFluidProperties::e_from_p_T(), StiffenedGasFluidProperties::e_from_p_T(), SimpleFluidProperties::e_from_p_T(), TabulatedFluidProperties::e_from_p_T(), SinglePhaseFluidProperties::e_from_p_T(), StiffenedGasFluidProperties::e_from_T_v(), IdealGasFluidProperties::e_from_T_v(), IdealGasFluidProperties::e_from_v_h(), StiffenedGasFluidProperties::e_from_v_h(), IdealGasFluidProperties::g_from_v_e(), StiffenedGasFluidProperties::g_from_v_e(), IdealGasFluidProperties::h_from_p_T(), NaClFluidProperties::h_from_p_T(), NitrogenFluidProperties::mu_from_rho_T(), HydrogenFluidProperties::mu_from_rho_T(), CO2FluidProperties::mu_from_rho_T(), StiffenedGasFluidProperties::p_from_T_v(), IdealGasFluidProperties::p_from_v_e(), StiffenedGasFluidProperties::p_from_v_e(), IdealGasFluidPropertiesPT::rho_e_dpT(), SinglePhaseFluidProperties::rho_e_dpT(), SinglePhaseFluidProperties::rho_e_from_p_T(), StiffenedGasFluidProperties::s_from_T_v(), IdealGasFluidProperties::s_from_v_e(), StiffenedGasFluidProperties::s_from_v_e(), Water97FluidProperties::subregion3(), Water97FluidProperties::subregionVolume(), SinglePhaseFluidProperties::T_from_p_h(), IdealGasFluidProperties::T_from_v_e(), StiffenedGasFluidProperties::T_from_v_e(), StiffenedGasFluidProperties::v_e_spndl_from_T(), and Water97FluidProperties::vaporTemperature().

293 {
294  mooseDeprecated(name(), ": e() is deprecated. Use e_from_p_T() instead");
295 
296  return e_from_p_T(p, T);
297 }
virtual Real e_from_p_T(Real p, Real T) const
Internal energy from pressure and temperature.
const std::string name
Definition: Setup.h:22

◆ e_dpT()

void SinglePhaseFluidProperties::e_dpT ( Real  pressure,
Real  temperature,
Real &  e,
Real &  de_dp,
Real &  de_dT 
) const
virtualinherited

Definition at line 300 of file SinglePhaseFluidProperties.C.

301 {
302  mooseDeprecated(name(), ": e_dpT() is deprecated. Use e_from_p_T() instead");
303 
304  e_from_p_T(p, T, e, de_dp, de_dT);
305 }
virtual Real e_from_p_T(Real p, Real T) const
Internal energy from pressure and temperature.
const std::string name
Definition: Setup.h:22
virtual Real e(Real pressure, Real temperature) const

◆ e_from_p_T() [1/2]

Real SinglePhaseFluidProperties::e_from_p_T ( Real  p,
Real  T 
) const
virtualinherited

◆ e_from_p_T() [2/2]

void SinglePhaseFluidProperties::e_from_p_T ( Real  p,
Real  T,
Real &  e,
Real &  de_dp,
Real &  de_dT 
) const
virtualinherited

Internal energy and its derivatives from pressure and temperature.

Parameters
[in]ppressure (Pa)
[in]Ttemperature (K)
[out]einternal energy (J/kg)
[out]de_dpderivative of internal energy w.r.t. pressure
[out]de_dTderivative of internal energy w.r.t. temperature

Reimplemented in TabulatedFluidProperties, SimpleFluidProperties, StiffenedGasFluidProperties, IdealGasFluidProperties, NaClFluidProperties, Water97FluidProperties, IdealGasFluidPropertiesPT, and HelmholtzFluidProperties.

Definition at line 42 of file SinglePhaseFluidProperties.C.

43 {
44  // From rho(p,T), compute: drho(p,T)/dp, drho(p,T)/dT
45  Real rho = 0., drho_dp = 0., drho_dT = 0.;
46  rho_from_p_T(p, T, rho, drho_dp, drho_dT);
47 
48  // From e(p, rho), compute: de(p,rho)/dp, de(p,rho)/drho
49  Real depr_dp = 0., depr_drho = 0.;
50  e_from_p_rho(p, rho, e, depr_dp, depr_drho);
51 
52  // Using partial derivative rules, we have:
53  // de(p,T)/dp = de(p,rho)/dp * dp/dp + de(p,rho)/drho * drho(p,T)/dp, (dp/dp == 1)
54  // de(p,T)/dT = de(p,rho)/dp * dp/dT + de(p,rho)/drho * drho(p,T)/dT, (dp/dT == 0)
55  de_dp = depr_dp + depr_drho * drho_dp;
56  de_dT = depr_drho * drho_dT;
57 }
virtual Real e(Real pressure, Real temperature) const

◆ e_spndl_from_v()

Real SinglePhaseFluidProperties::e_spndl_from_v ( Real  v) const
virtualinherited

Specific internal energy from temperature and specific volume.

Parameters
[in]Ttemperature
[in]vspecific volume

Reimplemented in StiffenedGasFluidProperties.

Definition at line 452 of file SinglePhaseFluidProperties.C.

Referenced by IdealRealGasMixtureFluidProperties::p_T_from_v_e().

453 {
454  mooseError(name(), ": ", __PRETTY_FUNCTION__, " not implemented.");
455 }
const std::string name
Definition: Setup.h:22

◆ execute()

virtual void FluidProperties::execute ( )
inlinefinalvirtualinherited

Definition at line 27 of file FluidProperties.h.

27 {}

◆ finalize()

virtual void FluidProperties::finalize ( )
inlinefinalvirtualinherited

Definition at line 29 of file FluidProperties.h.

29 {}

◆ fluidName()

std::string SinglePhaseFluidProperties::fluidName ( ) const
virtualinherited

◆ gamma_from_p_T()

Real SinglePhaseFluidProperties::gamma_from_p_T ( Real  pressure,
Real  temperature 
) const
virtualinherited

Adiabatic index - ratio of specific heats.

Parameters
pressurefluid pressure (Pa)
temperaturefluid temperature (K)
Returns
gamma (-)

Definition at line 149 of file SinglePhaseFluidProperties.C.

150 {
151  return cp_from_p_T(p, T) / cv_from_p_T(p, T);
152 }

◆ getNaN() [1/2]

Real NaNInterface::getNaN ( ) const
inlineprotectedinherited

Produces errors, warnings, or just quiet NaNs.

Definition at line 49 of file NaNInterface.h.

Referenced by NaNInterface::getNaN(), p_from_v_e(), IdealRealGasMixtureFluidProperties::v_from_p_T(), and IdealRealGasMixtureFluidProperties::xs_prim_from_p_T().

49 { return getNaN("A NaN was produced."); }
Real getNaN() const
Produces errors, warnings, or just quiet NaNs.
Definition: NaNInterface.h:49

◆ getNaN() [2/2]

template<typename... Args>
Real NaNInterface::getNaN ( Args &&...  args) const
inlineprotectedinherited

Definition at line 52 of file NaNInterface.h.

53  {
54  switch (_emit_on_nan)
55  {
56  case (NAN_MESSAGE_WARNING):
57  mooseWarning(_moose_object->name(), ": ", std::forward<Args>(args)...);
58  break;
59  case (NAN_MESSAGE_ERROR):
60  mooseError(_moose_object->name(), ": ", std::forward<Args>(args)...);
61  break;
62  default:
63  break;
64  }
65  // return a quiet NaN
66  return std::nan("");
67  }
const MooseObject * _moose_object
Definition: NaNInterface.h:41
enum NaNMessage _emit_on_nan
Raise mooseWarning or mooseError?
Definition: NaNInterface.h:44

◆ h()

Real SinglePhaseFluidProperties::h ( Real  p,
Real  T 
) const
virtualinherited

◆ h_dpT()

void SinglePhaseFluidProperties::h_dpT ( Real  pressure,
Real  temperature,
Real &  h,
Real &  dh_dp,
Real &  dh_dT 
) const
virtualinherited

Specific enthalpy and its derivatives from pressure and temperature.

Parameters
[in]ppressure (Pa)
[in]Ttemperature (K)
[out]hspecific enthalpy (J/kg)
[out]dh_dpderivative of specific enthalpy w.r.t. pressure
[out]dh_dTderivative of specific enthalpy w.r.t. temperature

Definition at line 437 of file SinglePhaseFluidProperties.C.

438 {
439  mooseDeprecated(name(), ": h_dpT() is deprecated. Use h_from_p_T() instead");
440 
441  h_from_p_T(p, T, h, dh_dp, dh_dT);
442 }
virtual Real h(Real p, Real T) const
Specific enthalpy from pressure and temperature.
const std::string name
Definition: Setup.h:22

◆ henryConstant() [1/2]

Real SinglePhaseFluidProperties::henryConstant ( Real  temperature) const
virtualinherited

Henry's law constant for dissolution in water.

Parameters
temperaturefluid temperature (K)
Returns
Henry's constant

Reimplemented in CO2FluidProperties, TabulatedFluidProperties, SimpleFluidProperties, IdealGasFluidPropertiesPT, HydrogenFluidProperties, NitrogenFluidProperties, and MethaneFluidProperties.

Definition at line 244 of file SinglePhaseFluidProperties.C.

Referenced by PorousFlowWaterNCG::enthalpyOfDissolution(), PorousFlowWaterNCG::equilibriumMassFractions(), TabulatedFluidProperties::henryConstant(), PorousFlowBrineCO2::henryConstant(), and SinglePhaseFluidProperties::henryConstant_dT().

245 {
246  mooseError(name(), ": henryConstant() is not implemented");
247 }
const std::string name
Definition: Setup.h:22

◆ henryConstant() [2/2]

void SinglePhaseFluidProperties::henryConstant ( Real  temperature,
Real &  Kh,
Real &  dKh_dT 
) const
virtualinherited

Henry's law constant for dissolution in water and derivative wrt temperature.

Parameters
temperaturefluid temperature (K)
[out]KhHenry's constant
[out]dKh_dTderivative of Kh wrt temperature

Reimplemented in CO2FluidProperties, TabulatedFluidProperties, SimpleFluidProperties, IdealGasFluidPropertiesPT, HydrogenFluidProperties, NitrogenFluidProperties, and MethaneFluidProperties.

Definition at line 250 of file SinglePhaseFluidProperties.C.

251 {
252  mooseError(name(), ": henryConstant() is not implemented");
253 }
const std::string name
Definition: Setup.h:22

◆ henryConstant_dT()

void SinglePhaseFluidProperties::henryConstant_dT ( Real  temperature,
Real &  Kh,
Real &  dKh_dT 
) const
virtualinherited

Definition at line 256 of file SinglePhaseFluidProperties.C.

257 {
258  mooseDeprecated(name(), ": henryConstant_dT() is deprecated. Use henryConstant() instead");
259 
260  henryConstant(T, Kh, dKh_dT);
261 }
const std::string name
Definition: Setup.h:22
virtual Real henryConstant(Real temperature) const
Henry&#39;s law constant for dissolution in water.

◆ henryConstantIAPWS() [1/2]

Real SinglePhaseFluidProperties::henryConstantIAPWS ( Real  temperature,
Real  A,
Real  B,
Real  C 
) const
protectedvirtualinherited

IAPWS formulation of Henry's law constant for dissolution in water From 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 161 of file SinglePhaseFluidProperties.C.

Referenced by MethaneFluidProperties::henryConstant(), NitrogenFluidProperties::henryConstant(), HydrogenFluidProperties::henryConstant(), CO2FluidProperties::henryConstant(), and SinglePhaseFluidProperties::henryConstantIAPWS_dT().

162 {
163  const Real Tr = T / 647.096;
164  const Real tau = 1.0 - Tr;
165 
166  const Real lnkh =
167  A / Tr + B * std::pow(tau, 0.355) / Tr + C * std::pow(Tr, -0.41) * std::exp(tau);
168 
169  // The vapor pressure used in this formulation
170  const std::vector<Real> a{
171  -7.85951783, 1.84408259, -11.7866497, 22.6807411, -15.9618719, 1.80122502};
172  const std::vector<Real> b{1.0, 1.5, 3.0, 3.5, 4.0, 7.5};
173  Real sum = 0.0;
174 
175  for (std::size_t i = 0; i < a.size(); ++i)
176  sum += a[i] * std::pow(tau, b[i]);
177 
178  return 22.064e6 * std::exp(sum / Tr) * std::exp(lnkh);
179 }
ExpressionBuilder::EBTerm pow(const ExpressionBuilder::EBTerm &left, T exponent)

◆ henryConstantIAPWS() [2/2]

void SinglePhaseFluidProperties::henryConstantIAPWS ( Real  temperature,
Real &  Kh,
Real &  dKh_dT,
Real  A,
Real  B,
Real  C 
) const
protectedvirtualinherited

Definition at line 182 of file SinglePhaseFluidProperties.C.

184 {
185  const Real pc = 22.064e6;
186  const Real Tc = 647.096;
187 
188  const Real Tr = T / Tc;
189  const Real tau = 1.0 - Tr;
190 
191  const Real lnkh =
192  A / Tr + B * std::pow(tau, 0.355) / Tr + C * std::pow(Tr, -0.41) * std::exp(tau);
193  const Real dlnkh_dT =
194  (-A / Tr / Tr - B * std::pow(tau, 0.355) / Tr / Tr - 0.355 * B * std::pow(tau, -0.645) / Tr -
195  0.41 * C * std::pow(Tr, -1.41) * std::exp(tau) - C * std::pow(Tr, -0.41) * std::exp(tau)) /
196  Tc;
197 
198  // The vapor pressure used in this formulation
199  const std::vector<Real> a{
200  -7.85951783, 1.84408259, -11.7866497, 22.6807411, -15.9618719, 1.80122502};
201  const std::vector<Real> b{1.0, 1.5, 3.0, 3.5, 4.0, 7.5};
202  Real sum = 0.0;
203  Real dsum = 0.0;
204 
205  for (std::size_t i = 0; i < a.size(); ++i)
206  {
207  sum += a[i] * std::pow(tau, b[i]);
208  dsum += a[i] * b[i] * std::pow(tau, b[i] - 1.0);
209  }
210 
211  const Real p = pc * std::exp(sum / Tr);
212  const Real dp_dT = -p / Tc / Tr * (sum / Tr + dsum);
213 
214  // Henry's constant and its derivative wrt temperature
215  Kh = p * std::exp(lnkh);
216  dKh_dT = (p * dlnkh_dT + dp_dT) * std::exp(lnkh);
217 }
ExpressionBuilder::EBTerm pow(const ExpressionBuilder::EBTerm &left, T exponent)

◆ henryConstantIAPWS_dT()

void SinglePhaseFluidProperties::henryConstantIAPWS_dT ( Real  temperature,
Real &  Kh,
Real &  dKh_dT,
Real  A,
Real  B,
Real  C 
) const
protectedvirtualinherited

Definition at line 220 of file SinglePhaseFluidProperties.C.

222 {
223  mooseDeprecated(name(),
224  ":henryConstantIAPWS_dT() is deprecated. Use henryConstantIAPWS() instead");
225 
226  henryConstantIAPWS(T, Kh, dKh_dT, A, B, C);
227 }
const std::string name
Definition: Setup.h:22
virtual Real henryConstantIAPWS(Real temperature, Real A, Real B, Real C) const
IAPWS formulation of Henry&#39;s law constant for dissolution in water From Guidelines on the Henry&#39;s con...

◆ initialize()

virtual void FluidProperties::initialize ( )
inlinefinalvirtualinherited

Definition at line 28 of file FluidProperties.h.

28 {}

◆ k()

Real SinglePhaseFluidProperties::k ( Real  pressure,
Real  temperature 
) const
virtualinherited

Thermal conductivity.

Parameters
pressurefluid pressure (Pa)
temperaturefluid temperature (K)
Returns
thermal conductivity (W/m/K)

Definition at line 405 of file SinglePhaseFluidProperties.C.

Referenced by SinglePhaseFluidProperties::k_dpT(), IdealGasFluidPropertiesPT::k_from_p_T(), MethaneFluidProperties::k_from_p_T(), SimpleFluidProperties::k_from_p_T(), NitrogenFluidProperties::k_from_p_T(), NaClFluidProperties::k_from_p_T(), HydrogenFluidProperties::k_from_p_T(), IdealGasFluidProperties::k_from_p_T(), StiffenedGasFluidProperties::k_from_p_T(), TabulatedFluidProperties::k_from_p_T(), and CO2FluidProperties::k_from_p_T().

406 {
407  mooseDeprecated(name(), ": k() is deprecated. Use k_from_p_T() instead");
408 
409  return k_from_p_T(p, T);
410 }
const std::string name
Definition: Setup.h:22

◆ k_dpT()

void SinglePhaseFluidProperties::k_dpT ( Real  pressure,
Real  temperature,
Real &  k,
Real &  dk_dp,
Real &  dk_dT 
) const
virtualinherited

Thermal conductivity and its derivatives wrt pressure and temperature.

Parameters
pressurefluid pressure (Pa)
temperaturefluid temperature (K)
[out]thermalconductivity (W/m/K)
[out]derivativeof thermal conductivity wrt pressure
[out]derivativeof thermal conductivity wrt temperature

Definition at line 413 of file SinglePhaseFluidProperties.C.

414 {
415  mooseDeprecated(name(), ": k_dpT() is deprecated. Use k_from_p_T() instead");
416 
417  k_from_p_T(p, T, k, dk_dp, dk_dT);
418 }
virtual Real k(Real pressure, Real temperature) const
Thermal conductivity.
const std::string name
Definition: Setup.h:22

◆ molarMass()

Real SinglePhaseFluidProperties::molarMass ( ) const
virtualinherited

◆ mu()

Real SinglePhaseFluidProperties::mu ( Real  pressure,
Real  temperature 
) const
virtualinherited

Dynamic viscosity.

Parameters
pressurefluid pressure (Pa)
temperaturefluid temperature (K)
Returns
viscosity (Pa.s)

Definition at line 345 of file SinglePhaseFluidProperties.C.

Referenced by SinglePhaseFluidProperties::mu_dpT(), SinglePhaseFluidProperties::mu_drhoT_from_rho_T(), MethaneFluidProperties::mu_from_p_T(), CO2FluidProperties::mu_from_p_T(), NitrogenFluidProperties::mu_from_p_T(), HydrogenFluidProperties::mu_from_p_T(), IdealGasFluidPropertiesPT::mu_from_p_T(), IdealGasFluidProperties::mu_from_p_T(), Water97FluidProperties::mu_from_p_T(), StiffenedGasFluidProperties::mu_from_p_T(), SimpleFluidProperties::mu_from_p_T(), TabulatedFluidProperties::mu_from_p_T(), NitrogenFluidProperties::mu_from_rho_T(), HydrogenFluidProperties::mu_from_rho_T(), CO2FluidProperties::mu_from_rho_T(), Water97FluidProperties::mu_from_rho_T(), SinglePhaseFluidProperties::rho_mu(), SinglePhaseFluidProperties::rho_mu_dpT(), NitrogenFluidProperties::rho_mu_from_p_T(), HydrogenFluidProperties::rho_mu_from_p_T(), CO2FluidProperties::rho_mu_from_p_T(), IdealGasFluidPropertiesPT::rho_mu_from_p_T(), Water97FluidProperties::rho_mu_from_p_T(), and SinglePhaseFluidProperties::rho_mu_from_p_T().

346 {
347  mooseDeprecated(name(), ": mu() is deprecated. Use mu_from_p_T() instead");
348 
349  return mu_from_p_T(p, T);
350 }
const std::string name
Definition: Setup.h:22

◆ mu_dpT()

void SinglePhaseFluidProperties::mu_dpT ( Real  pressure,
Real  temperature,
Real &  mu,
Real &  dmu_dp,
Real &  dmu_dT 
) const
virtualinherited

Dynamic viscosity and its derivatives wrt pressure and temperature.

Parameters
pressurefluid pressure (Pa)
temperaturefluid temperature (K)
[out]muviscosity (Pa.s)
[out]dmu_dpderivative of viscosity wrt pressure
[out]dmu_dTderivative of viscosity wrt temperature

Definition at line 353 of file SinglePhaseFluidProperties.C.

354 {
355  mooseDeprecated(name(), ": mu_dpT() is deprecated. Use mu_from_p_T() instead");
356 
357  mu_from_p_T(p, T, mu, dmu_dp, dmu_dT);
358 }
virtual Real mu(Real pressure, Real temperature) const
Dynamic viscosity.
const std::string name
Definition: Setup.h:22

◆ mu_drhoT_from_rho_T()

void SinglePhaseFluidProperties::mu_drhoT_from_rho_T ( Real  density,
Real  temperature,
Real  ddensity_dT,
Real &  mu,
Real &  dmu_drho,
Real &  dmu_dT 
) const
virtualinherited

Definition at line 236 of file SinglePhaseFluidProperties.C.

238 {
239  mooseDeprecated(name(), ":mu_drhoT_from_rho_T() is deprecated. Use mu_from_rho_T() instead");
240 
241  mu_from_rho_T(rho, T, drho_dT, mu, dmu_drho, dmu_dT);
242 }
virtual Real mu(Real pressure, Real temperature) const
Dynamic viscosity.
const std::string name
Definition: Setup.h:22
virtual void mu_from_rho_T(Real density, Real temperature, Real ddensity_dT, Real &mu, Real &dmu_drho, Real &dmu_dT) const
Dynamic viscosity and its derivatives wrt density and temperature TODO: this shouldn&#39;t need 3 input a...

◆ mu_from_rho_T()

void SinglePhaseFluidProperties::mu_from_rho_T ( Real  density,
Real  temperature,
Real  ddensity_dT,
Real &  mu,
Real &  dmu_drho,
Real &  dmu_dT 
) const
virtualinherited

Dynamic viscosity and its derivatives wrt density and temperature TODO: this shouldn't need 3 input args - AD will assume/call the 2-input version.

Parameters
densityfluid density (kg/m^3)
temperaturefluid temperature (K)
ddensity_dTderivative of density wrt temperature
[out]muviscosity (Pa.s)
[out]dmu_drhoderivative of viscosity wrt density
[out]dmu_dTderivative of viscosity wrt temperature

Reimplemented in Water97FluidProperties, CO2FluidProperties, HydrogenFluidProperties, and NitrogenFluidProperties.

Definition at line 230 of file SinglePhaseFluidProperties.C.

Referenced by SinglePhaseFluidProperties::mu_drhoT_from_rho_T().

231 {
232  mooseError(name(), ": mu_from_rho_T is not implemented.");
233 }
const std::string name
Definition: Setup.h:22

◆ p_from_v_e() [1/2]

Real NaNInterfaceTestFluidProperties::p_from_v_e ( Real  v,
Real  e 
) const
overridevirtual

Definition at line 32 of file NaNInterfaceTestFluidProperties.C.

Referenced by NaNInterfaceTestKernel::computeQpResidual().

33 {
34  return getNaN();
35 }
Real getNaN() const
Produces errors, warnings, or just quiet NaNs.
Definition: NaNInterface.h:49

◆ p_from_v_e() [2/2]

void NaNInterfaceTestFluidProperties::p_from_v_e ( Real  v,
Real  e,
Real &  p,
Real &  dp_dv,
Real &  dp_de 
) const
overridevirtual

Definition at line 38 of file NaNInterfaceTestFluidProperties.C.

39 {
40 }

◆ propfunc() [1/15]

SinglePhaseFluidProperties::propfunc ( p  ,
v  ,
e   
)
inherited

Compute a fluid property given for the state defined by two given properties.

For all functions, the first two arguments are the given properties that define the fluid state. For the two-argument variants, the desired property is the return value. The five-argument variants also provide partial derivatives dx/da and dx/db where x is the desired property being computed, a is the first given property, and b is the second given property. The desired property, dx/da, and dx/db are stored into the 3rd, 4th, and 5th arguments respectively.

Properties/parameters used in these function are listed below with their units:

p pressure [Pa] T temperature [K] e specific internal energy [J/kg] v specific volume [m^3/kg] rho density [kg/m^3] h specific enthalpy [J/kg] s specific entropy [J/(kg*K)] mu viscosity [Pa*s] k thermal conductivity [W/(m*K)] c speed of sound [m/s] cp constant-pressure specific heat [J/K] cv constant-volume specific heat [J/K] beta volumetric thermal expansion coefficient [1/K] g Gibbs free energy [J] pp_sat partial pressure at saturation [Pa]

As an example:

// calculate pressure given specific vol and energy: auto pressure = your_fluid_properties_object.p_from_v_e(specific_vol, specific_energy);

// or use the derivative variant: Real dp_dv = 0; // derivative will be stored into here Real dp_de = 0; // derivative will be stored into here your_fluid_properties_object.p_from_v_e(specific_vol, specific_energy, pressure, dp_dv, dp_de);

Automatic differentiation (AD) support is provided through x_from_a_b(DualReal a, DualReal b) versions of the functions where a and b must be ADReal/DualNumber's calculated using all AD-supporting values:

auto v = 1/rho; // rho must be an AD non-linear variable. auto e = rhoE/rho - vel_energy; // rhoE and vel_energy must be AD variables/numbers also. auto pressure = your_fluid_properties_object.p_from_v_e(v, e); // pressure now contains partial derivatives w.r.t. all degrees of freedom

◆ propfunc() [2/15]

e SinglePhaseFluidProperties::propfunc ( c  ,
v  ,
e   
)
inherited

◆ propfunc() [3/15]

e e SinglePhaseFluidProperties::propfunc ( cv  ,
v  ,
e   
)
inherited

◆ propfunc() [4/15]

e e e SinglePhaseFluidProperties::propfunc ( k  ,
v  ,
e   
)
inherited

◆ propfunc() [5/15]

e e e e SinglePhaseFluidProperties::propfunc ( s  ,
h  ,
p   
)
inherited

◆ propfunc() [6/15]

e e e e s SinglePhaseFluidProperties::propfunc ( e  ,
v  ,
h   
)
inherited

◆ propfunc() [7/15]

e e e e s T SinglePhaseFluidProperties::propfunc ( pp_sat  ,
p  ,
T   
)
inherited

◆ propfunc() [8/15]

e e e e s T T SinglePhaseFluidProperties::propfunc ( k  ,
rho  ,
T   
)
inherited

◆ propfunc() [9/15]

e e e e s T T T SinglePhaseFluidProperties::propfunc ( cp  ,
p  ,
T   
)
inherited

◆ propfunc() [10/15]

e e e e s T T T T SinglePhaseFluidProperties::propfunc ( mu  ,
p  ,
T   
)
inherited

◆ propfunc() [11/15]

e e e e s T T T T T SinglePhaseFluidProperties::propfunc ( rho  ,
p  ,
T   
)
inherited

◆ propfunc() [12/15]

e e e e s T T T T T rho SinglePhaseFluidProperties::propfunc ( e  ,
T  ,
v   
)
inherited

◆ propfunc() [13/15]

e e e e s T T T T T rho v SinglePhaseFluidProperties::propfunc ( h  ,
T  ,
v   
)
inherited

◆ propfunc() [14/15]

e e e e s T T T T T rho v v SinglePhaseFluidProperties::propfunc ( cv  ,
T  ,
v   
)
inherited

◆ propfunc() [15/15]

e e e e s T T T T T rho v v T SinglePhaseFluidProperties::propfunc ( p  ,
h  ,
s   
)
inherited

◆ rho()

virtual Real SinglePhaseFluidProperties::rho ( Real  p,
Real  T 
) const
virtualinherited

Density from pressure and temperature.

Parameters
[in]ppressure (Pa)
[in]Ttemperature (K)
Returns
density (kg/m^3)

◆ rho_dpT()

void SinglePhaseFluidProperties::rho_dpT ( Real  pressure,
Real  temperature,
Real &  rho,
Real &  drho_dp,
Real &  drho_dT 
) const
virtualinherited

Density and its derivatives from pressure and temperature.

Parameters
[in]ppressure (Pa)
[in]Ttemperature (K)
[out]rhodensity (kg/m^3)
[out]drho_dpderivative of density w.r.t. pressure
[out]drho_dTderivative of density w.r.t. temperature

Definition at line 283 of file SinglePhaseFluidProperties.C.

285 {
286  mooseDeprecated(name(), ": rho_dpT() is deprecated. Use rho_from_p_T() instead");
287 
288  rho_from_p_T(p, T, rho, drho_dp, drho_dT);
289 }
const std::string name
Definition: Setup.h:22

◆ rho_e_dpT()

void SinglePhaseFluidProperties::rho_e_dpT ( Real  pressure,
Real  temperature,
Real &  rho,
Real &  drho_dp,
Real &  drho_dT,
Real &  e,
Real &  de_dp,
Real &  de_dT 
) const
virtualinherited

Reimplemented in IdealGasFluidPropertiesPT.

Definition at line 322 of file SinglePhaseFluidProperties.C.

330 {
331  mooseDeprecated(name(), ": rho_e_dpT() is deprecated. Use rho_e_from_p_T() instead");
332 
333  rho_e_from_p_T(p, T, rho, drho_dp, drho_dT, e, de_dp, de_dT);
334 }
virtual void rho_e_from_p_T(Real pressure, Real temperature, Real &rho, Real &drho_dp, Real &drho_dT, Real &e, Real &de_dp, Real &de_dT) const
Density and internal energy and their derivatives wrt pressure and temperature.
const std::string name
Definition: Setup.h:22
virtual Real e(Real pressure, Real temperature) const

◆ rho_e_from_p_T()

void SinglePhaseFluidProperties::rho_e_from_p_T ( Real  pressure,
Real  temperature,
Real &  rho,
Real &  drho_dp,
Real &  drho_dT,
Real &  e,
Real &  de_dp,
Real &  de_dT 
) const
virtualinherited

Density and internal energy and their derivatives wrt pressure and temperature.

Parameters
pressurefluid pressure (Pa)
temperaturefluid temperature (K)
[out]rhodensity (kg/m^3)
[out]drho_dpderivative of density wrt pressure
[out]drho_dTderivative of density wrt temperature
[out]einternal energy (J/kg)
[out]de_dpderivative of internal energy wrt pressure
[out]de_dTderivative of internal energy wrt temperature

Definition at line 308 of file SinglePhaseFluidProperties.C.

Referenced by SinglePhaseFluidProperties::rho_e_dpT().

316 {
317  rho_from_p_T(p, T, rho, drho_dp, drho_dT);
318  e_from_p_T(p, T, e, de_dp, de_dT);
319 }
virtual Real e_from_p_T(Real p, Real T) const
Internal energy from pressure and temperature.
virtual Real e(Real pressure, Real temperature) const

◆ rho_mu()

void SinglePhaseFluidProperties::rho_mu ( Real  pressure,
Real  temperature,
Real &  rho,
Real &  mu 
) const
virtualinherited

Density and viscosity.

Parameters
pressurefluid pressure (Pa)
temperaturefluid temperature (K)
[out]rhodensity (kg/m^3)
[out]muviscosity (Pa.s)

Definition at line 361 of file SinglePhaseFluidProperties.C.

362 {
363  mooseDeprecated(name(), ": rho_mu() is deprecated. Use rho_mu_from_p_T() instead");
364 
365  rho_mu_from_p_T(p, T, rho, mu);
366 }
virtual Real mu(Real pressure, Real temperature) const
Dynamic viscosity.
const std::string name
Definition: Setup.h:22
virtual void rho_mu_from_p_T(Real pressure, Real temperature, Real &rho, Real &mu) const

◆ rho_mu_dpT()

void SinglePhaseFluidProperties::rho_mu_dpT ( Real  pressure,
Real  temperature,
Real &  rho,
Real &  drho_dp,
Real &  drho_dT,
Real &  mu,
Real &  dmu_dp,
Real &  dmu_dT 
) const
virtualinherited

Definition at line 376 of file SinglePhaseFluidProperties.C.

384 {
385  mooseDeprecated(name(), ": rho_mu_dpT() is deprecated. Use rho_mu_from_p_T() instead");
386 
387  rho_mu_from_p_T(p, T, rho, drho_dp, drho_dT, mu, dmu_dp, dmu_dT);
388 }
virtual Real mu(Real pressure, Real temperature) const
Dynamic viscosity.
const std::string name
Definition: Setup.h:22
virtual void rho_mu_from_p_T(Real pressure, Real temperature, Real &rho, Real &mu) const

◆ rho_mu_from_p_T() [1/2]

void SinglePhaseFluidProperties::rho_mu_from_p_T ( Real  pressure,
Real  temperature,
Real &  rho,
Real &  mu 
) const
virtualinherited

◆ rho_mu_from_p_T() [2/2]

void SinglePhaseFluidProperties::rho_mu_from_p_T ( Real  pressure,
Real  temperature,
Real &  rho,
Real &  drho_dp,
Real &  drho_dT,
Real &  mu,
Real &  dmu_dp,
Real &  dmu_dT 
) const
virtualinherited

Density and viscosity and their derivatives wrt pressure and temperature.

Parameters
pressurefluid pressure (Pa)
temperaturefluid temperature (K)
[out]rhodensity (kg/m^3)
[out]drho_dpderivative of density wrt pressure
[out]drho_dTderivative of density wrt temperature
[out]muviscosity (Pa.s)
[out]dmu_dpderivative of viscosity wrt pressure
[out]dmu_dTderivative of viscosity wrt temperature

Reimplemented in Water97FluidProperties, IdealGasFluidPropertiesPT, CO2FluidProperties, HydrogenFluidProperties, and NitrogenFluidProperties.

Definition at line 391 of file SinglePhaseFluidProperties.C.

399 {
400  rho_from_p_T(p, T, rho, drho_dp, drho_dT);
401  mu_from_p_T(p, T, mu, dmu_dp, dmu_dT);
402 }
virtual Real mu(Real pressure, Real temperature) const
Dynamic viscosity.

◆ s()

Real SinglePhaseFluidProperties::s ( Real  pressure,
Real  temperature 
) const
virtualinherited

◆ subdomainSetup()

virtual void FluidProperties::subdomainSetup ( )
inlinefinalvirtualinherited

Definition at line 32 of file FluidProperties.h.

32 {}

◆ T_from_p_h()

Real SinglePhaseFluidProperties::T_from_p_h ( Real  pressure,
Real  enthalpy 
) const
virtualinherited

Temperature from pressure and specific enthalpy.

Parameters
[in]pressurepressure (Pa)
[in]enthalpyenthalpy (J/kg)
Returns
Temperature (K)

Reimplemented in IdealGasFluidProperties.

Definition at line 464 of file SinglePhaseFluidProperties.C.

465 {
466  const Real s = s_from_h_p(h, p);
467  const Real rho = rho_from_p_s(p, s);
468  const Real v = 1. / rho;
469  const Real e = e_from_v_h(v, h);
470  return T_from_v_e(v, e);
471 }
e e e e s T T T T T rho v v T virtual e Real s(Real pressure, Real temperature) const
virtual Real h(Real p, Real T) const
Specific enthalpy from pressure and temperature.
virtual Real e(Real pressure, Real temperature) const

◆ threadJoin()

virtual void FluidProperties::threadJoin ( const UserObject &  )
inlinefinalvirtualinherited

Definition at line 31 of file FluidProperties.h.

31 {}

◆ triplePointPressure()

Real SinglePhaseFluidProperties::triplePointPressure ( ) const
virtualinherited

Triple point pressure.

Returns
triple point pressure (Pa)

Reimplemented in HydrogenFluidProperties, CO2FluidProperties, NitrogenFluidProperties, MethaneFluidProperties, NaClFluidProperties, and Water97FluidProperties.

Definition at line 137 of file SinglePhaseFluidProperties.C.

138 {
139  mooseError(name(), ": triplePointPressure() is not implemented");
140 }
const std::string name
Definition: Setup.h:22

◆ triplePointTemperature()

Real SinglePhaseFluidProperties::triplePointTemperature ( ) const
virtualinherited

Triple point temperature.

Returns
triple point temperature (K)

Reimplemented in HydrogenFluidProperties, CO2FluidProperties, NitrogenFluidProperties, MethaneFluidProperties, NaClFluidProperties, and Water97FluidProperties.

Definition at line 143 of file SinglePhaseFluidProperties.C.

144 {
145  mooseError(name(), ": triplePointTemperature() is not implemented");
146 }
const std::string name
Definition: Setup.h:22

◆ v_e_spndl_from_T()

void SinglePhaseFluidProperties::v_e_spndl_from_T ( Real  T,
Real &  v,
Real &  e 
) const
virtualinherited

Specific internal energy from temperature and specific volume.

Parameters
[in]Ttemperature
[in]vspecific volume

Reimplemented in StiffenedGasFluidProperties.

Definition at line 458 of file SinglePhaseFluidProperties.C.

Referenced by IdealRealGasMixtureFluidProperties::v_from_p_T().

459 {
460  mooseError(name(), ": ", __PRETTY_FUNCTION__, " not implemented.");
461 }
const std::string name
Definition: Setup.h:22

◆ v_from_p_T() [1/2]

Real SinglePhaseFluidProperties::v_from_p_T ( Real  p,
Real  T 
) const
virtualinherited

◆ v_from_p_T() [2/2]

void SinglePhaseFluidProperties::v_from_p_T ( Real  p,
Real  T,
Real &  v,
Real &  dv_dp,
Real &  dv_dT 
) const
virtualinherited

Specific volume and its derivatives from pressure and temperature.

Parameters
[in]ppressure
[in]Ttemperature
[out]vspecific volume
[out]dv_dpderivative of specific volume w.r.t. pressure
[out]dv_dTderivative of specific volume w.r.t. temperature

Definition at line 67 of file SinglePhaseFluidProperties.C.

68 {
69  Real rho, drho_dp, drho_dT;
70  rho_from_p_T(p, T, rho, drho_dp, drho_dT);
71 
72  v = 1.0 / rho;
73  const Real dv_drho = -1.0 / (rho * rho);
74 
75  dv_dp = dv_drho * drho_dp;
76  dv_dT = dv_drho * drho_dT;
77 }

◆ vaporPressure() [1/2]

Real SinglePhaseFluidProperties::vaporPressure ( Real  temperature) const
virtualinherited

Vapor pressure.

Used to delineate liquid and gas phases. Valid for temperatures between the triple point temperature and the critical temperature

Parameters
temperaturewater temperature (K)
Returns
saturation pressure (Pa)

Reimplemented in TabulatedFluidProperties, Water97FluidProperties, CO2FluidProperties, HydrogenFluidProperties, NitrogenFluidProperties, and MethaneFluidProperties.

Definition at line 263 of file SinglePhaseFluidProperties.C.

Referenced by PorousFlowWaterNCG::equilibriumMassFractions(), PorousFlowWaterNCG::gasProperties(), BrineFluidProperties::vaporPressure(), TabulatedFluidProperties::vaporPressure(), and SinglePhaseFluidProperties::vaporPressure_dT().

264 {
265  mooseError(name(), ": vaporPressure() is not implemented");
266 }
const std::string name
Definition: Setup.h:22

◆ vaporPressure() [2/2]

void SinglePhaseFluidProperties::vaporPressure ( Real  temperature,
Real &  psat,
Real &  dpsat_dT 
) const
virtualinherited

Vapor pressure.

Used to delineate liquid and gas phases. Valid for temperatures between the triple point temperature and the critical temperature

Parameters
temperaturewater temperature (K)
[out]saturationpressure (Pa)
[out]derivativeof saturation pressure wrt temperature (Pa/K)

Reimplemented in TabulatedFluidProperties, Water97FluidProperties, CO2FluidProperties, HydrogenFluidProperties, NitrogenFluidProperties, and MethaneFluidProperties.

Definition at line 269 of file SinglePhaseFluidProperties.C.

270 {
271  mooseError(name(), ": vaporPressure() is not implemented");
272 }
const std::string name
Definition: Setup.h:22

◆ vaporPressure_dT()

void SinglePhaseFluidProperties::vaporPressure_dT ( Real  temperature,
Real &  psat,
Real &  dpsat_dT 
) const
virtualinherited

Definition at line 275 of file SinglePhaseFluidProperties.C.

276 {
277  mooseDeprecated(name(), ": vaporPressure_dT() is deprecated. Use vaporPressure() instead");
278 
279  vaporPressure(T, psat, dpsat_dT);
280 }
virtual Real vaporPressure(Real temperature) const
Vapor pressure.
const std::string name
Definition: Setup.h:22

Member Data Documentation

◆ _emit_on_nan

enum NaNMessage NaNInterface::_emit_on_nan
protectedinherited

Raise mooseWarning or mooseError?

Definition at line 44 of file NaNInterface.h.

Referenced by NaNInterface::getNaN().

◆ _moose_object

const MooseObject* NaNInterface::_moose_object
protectedinherited

Definition at line 41 of file NaNInterface.h.

Referenced by NaNInterface::getNaN(), and NaNInterface::NaNInterface().

◆ _R

const Real SinglePhaseFluidProperties::_R
protectedinherited

◆ _T_c2k

const Real SinglePhaseFluidProperties::_T_c2k
protectedinherited

◆ p [1/7]

e e e e SinglePhaseFluidProperties::p
inherited

Definition at line 130 of file SinglePhaseFluidProperties.h.

Referenced by SinglePhaseFluidProperties::beta(), SinglePhaseFluidProperties::beta_from_p_T(), SinglePhaseFluidProperties::c(), StiffenedGasFluidProperties::c_from_v_e(), SinglePhaseFluidProperties::e(), SinglePhaseFluidProperties::e_dpT(), StiffenedGasFluidProperties::e_from_p_rho(), IdealGasFluidProperties::e_from_p_rho(), IdealGasFluidProperties::e_from_p_T(), StiffenedGasFluidProperties::e_from_p_T(), SinglePhaseFluidProperties::e_from_p_T(), IdealGasFluidProperties::g_from_v_e(), StiffenedGasFluidProperties::g_from_v_e(), SinglePhaseFluidProperties::gamma_from_p_T(), TabulatedFluidProperties::generateTabulatedData(), SinglePhaseFluidProperties::h(), SinglePhaseFluidProperties::h_dpT(), IdealGasFluidProperties::h_from_p_T(), StiffenedGasFluidProperties::h_from_p_T(), SinglePhaseFluidProperties::henryConstantIAPWS(), SinglePhaseFluidProperties::k(), SinglePhaseFluidProperties::k_dpT(), SinglePhaseFluidProperties::mu(), SinglePhaseFluidProperties::mu_dpT(), IdealGasFluidProperties::p_from_h_s(), StiffenedGasFluidProperties::p_from_h_s(), StiffenedGasFluidProperties::p_from_T_v(), IdealGasFluidProperties::p_from_T_v(), IdealGasFluidProperties::p_from_v_e(), StiffenedGasFluidProperties::p_from_v_e(), SinglePhaseFluidProperties::rho_dpT(), SinglePhaseFluidProperties::rho_e_dpT(), SinglePhaseFluidProperties::rho_e_from_p_T(), StiffenedGasFluidProperties::rho_from_p_s(), IdealGasFluidProperties::rho_from_p_s(), StiffenedGasFluidProperties::rho_from_p_T(), IdealGasFluidProperties::rho_from_p_T(), SinglePhaseFluidProperties::rho_mu(), SinglePhaseFluidProperties::rho_mu_dpT(), SinglePhaseFluidProperties::rho_mu_from_p_T(), SinglePhaseFluidProperties::s(), StiffenedGasFluidProperties::s_from_h_p(), IdealGasFluidProperties::s_from_h_p(), IdealGasFluidProperties::s_from_p_T(), StiffenedGasFluidProperties::s_from_p_T(), IdealGasFluidPropertiesPT::s_from_p_T(), SimpleFluidProperties::s_from_p_T(), Water97FluidProperties::s_from_p_T(), TabulatedFluidProperties::s_from_p_T(), IdealGasFluidProperties::s_from_T_v(), StiffenedGasFluidProperties::s_from_v_e(), IdealGasFluidProperties::s_from_v_e(), SinglePhaseFluidProperties::T_from_p_h(), SinglePhaseFluidProperties::v_from_p_T(), Water97FluidProperties::vaporPressure(), and TabulatedFluidProperties::writeTabulatedData().

◆ p [2/7]

e e e e s SinglePhaseFluidProperties::p
inherited

Definition at line 132 of file SinglePhaseFluidProperties.h.

◆ p [3/7]

e e e e s T T SinglePhaseFluidProperties::p
inherited

Definition at line 136 of file SinglePhaseFluidProperties.h.

◆ p [4/7]

e e e e s T T T SinglePhaseFluidProperties::p
inherited

Definition at line 138 of file SinglePhaseFluidProperties.h.

◆ p [5/7]

e e e e s T T T T SinglePhaseFluidProperties::p
inherited

Definition at line 140 of file SinglePhaseFluidProperties.h.

◆ p [6/7]

e e e e s T T T T T SinglePhaseFluidProperties::p
inherited

Definition at line 142 of file SinglePhaseFluidProperties.h.

◆ p [7/7]

e e e e s T T T T T rho v v SinglePhaseFluidProperties::p
inherited

Definition at line 148 of file SinglePhaseFluidProperties.h.

◆ rho

Real SinglePhaseFluidProperties::rho
inherited

Definition at line 134 of file SinglePhaseFluidProperties.h.

Referenced by SinglePhaseFluidProperties::beta_from_p_T(), StiffenedGasFluidProperties::c2_from_p_rho(), StiffenedGasFluidProperties::e_from_p_rho(), IdealGasFluidProperties::e_from_p_rho(), NaClFluidProperties::e_from_p_T(), SinglePhaseFluidProperties::e_from_p_T(), IdealGasFluidProperties::h_from_p_T(), Water97FluidProperties::k_from_p_T(), SinglePhaseFluidProperties::mu_drhoT_from_rho_T(), CO2FluidProperties::mu_from_p_T(), NitrogenFluidProperties::mu_from_p_T(), HydrogenFluidProperties::mu_from_p_T(), Water97FluidProperties::mu_from_p_T(), SinglePhaseFluidProperties::rho_dpT(), IdealGasFluidPropertiesPT::rho_e_dpT(), SinglePhaseFluidProperties::rho_e_dpT(), SinglePhaseFluidProperties::rho_e_from_p_T(), IdealGasFluidProperties::rho_from_p_s(), StiffenedGasFluidProperties::rho_from_p_s(), HelmholtzFluidProperties::rho_from_p_T(), CO2FluidProperties::rho_from_p_T(), StiffenedGasFluidProperties::rho_from_p_T(), IdealGasFluidPropertiesPT::rho_from_p_T(), IdealGasFluidProperties::rho_from_p_T(), Water97FluidProperties::rho_from_p_T(), NaClFluidProperties::rho_from_p_T(), SimpleFluidProperties::rho_from_p_T(), TabulatedFluidProperties::rho_from_p_T(), SinglePhaseFluidProperties::rho_mu(), SinglePhaseFluidProperties::rho_mu_dpT(), NitrogenFluidProperties::rho_mu_from_p_T(), HydrogenFluidProperties::rho_mu_from_p_T(), CO2FluidProperties::rho_mu_from_p_T(), IdealGasFluidPropertiesPT::rho_mu_from_p_T(), Water97FluidProperties::rho_mu_from_p_T(), SinglePhaseFluidProperties::rho_mu_from_p_T(), SinglePhaseFluidProperties::T_from_p_h(), and SinglePhaseFluidProperties::v_from_p_T().

◆ T [1/2]

e e e e s T T T T T rho SinglePhaseFluidProperties::T
inherited

Definition at line 144 of file SinglePhaseFluidProperties.h.

Referenced by SinglePhaseFluidProperties::beta(), SinglePhaseFluidProperties::beta_from_p_T(), SinglePhaseFluidProperties::c(), IdealGasFluidProperties::c_from_v_e(), SinglePhaseFluidProperties::e(), SinglePhaseFluidProperties::e_dpT(), IdealGasFluidProperties::e_from_p_T(), StiffenedGasFluidProperties::e_from_p_T(), SinglePhaseFluidProperties::e_from_p_T(), StiffenedGasFluidProperties::e_from_T_v(), IdealGasFluidProperties::e_from_T_v(), IdealGasFluidProperties::g_from_v_e(), StiffenedGasFluidProperties::g_from_v_e(), SinglePhaseFluidProperties::gamma_from_p_T(), SinglePhaseFluidProperties::h(), SinglePhaseFluidProperties::h_dpT(), IdealGasFluidProperties::h_from_p_T(), StiffenedGasFluidProperties::h_from_p_T(), StiffenedGasFluidProperties::h_from_T_v(), IdealGasFluidProperties::h_from_T_v(), SinglePhaseFluidProperties::henryConstant_dT(), SinglePhaseFluidProperties::henryConstantIAPWS(), SinglePhaseFluidProperties::henryConstantIAPWS_dT(), SinglePhaseFluidProperties::k(), SinglePhaseFluidProperties::k_dpT(), SinglePhaseFluidProperties::mu(), SinglePhaseFluidProperties::mu_dpT(), SinglePhaseFluidProperties::mu_drhoT_from_rho_T(), StiffenedGasFluidProperties::p_from_T_v(), IdealGasFluidProperties::p_from_T_v(), SinglePhaseFluidProperties::rho_dpT(), SinglePhaseFluidProperties::rho_e_dpT(), SinglePhaseFluidProperties::rho_e_from_p_T(), IdealGasFluidProperties::rho_from_p_s(), StiffenedGasFluidProperties::rho_from_p_s(), StiffenedGasFluidProperties::rho_from_p_T(), IdealGasFluidProperties::rho_from_p_T(), SinglePhaseFluidProperties::rho_mu(), SinglePhaseFluidProperties::rho_mu_dpT(), SinglePhaseFluidProperties::rho_mu_from_p_T(), SinglePhaseFluidProperties::s(), IdealGasFluidProperties::s_from_p_T(), StiffenedGasFluidProperties::s_from_p_T(), IdealGasFluidPropertiesPT::s_from_p_T(), SimpleFluidProperties::s_from_p_T(), Water97FluidProperties::s_from_p_T(), TabulatedFluidProperties::s_from_p_T(), StiffenedGasFluidProperties::s_from_T_v(), IdealGasFluidProperties::s_from_T_v(), StiffenedGasFluidProperties::s_from_v_e(), IdealGasFluidProperties::s_from_v_e(), IdealGasFluidProperties::T_from_v_e(), StiffenedGasFluidProperties::T_from_v_e(), SinglePhaseFluidProperties::v_from_p_T(), and SinglePhaseFluidProperties::vaporPressure_dT().

◆ T [2/2]

e e e e s T T T T T rho v SinglePhaseFluidProperties::T
inherited

Definition at line 146 of file SinglePhaseFluidProperties.h.

◆ v [1/5]

SinglePhaseFluidProperties::v
inherited

◆ v [2/5]

e SinglePhaseFluidProperties::v
inherited

Definition at line 124 of file SinglePhaseFluidProperties.h.

◆ v [3/5]

e e SinglePhaseFluidProperties::v
inherited

Definition at line 126 of file SinglePhaseFluidProperties.h.

◆ v [4/5]

e e e SinglePhaseFluidProperties::v
inherited

Definition at line 128 of file SinglePhaseFluidProperties.h.

◆ v [5/5]

e e e e s T T T T T rho v v T SinglePhaseFluidProperties::v
inherited

Definition at line 150 of file SinglePhaseFluidProperties.h.


The documentation for this class was generated from the following files: