SinglePhaseFluidProperties Class Reference

Common class for single phase fluid properties. More...

#include <SinglePhaseFluidProperties.h>

Inheritance diagram for SinglePhaseFluidProperties:

Public Member Functions
	SinglePhaseFluidProperties (const InputParameters &parameters)
virtual	~SinglePhaseFluidProperties ()
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 Real	rho (Real p, Real T) const
	Density from pressure and temperature. More...
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 Real	e (Real pressure, Real temperature) const
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 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 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

Protected Attributes
const Real	_R
	Universal gas constant (J/mol/K) More...
const Real	_T_c2k
	Conversion of temperature from Celsius to Kelvin. More...

Private Member Functions
template<typename... Args>
void	fluidPropError (Args... args) const

Private Attributes
bool	_allow_imperfect_jacobians
	v
e	v
e e	v
e e e	v
e e e e	p
e e e e s	p
e e e e s T	rho
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	T
e e e e s T T T T T rho v	T
e e e e s T T T T T rho v v	p
e e e e s T T T T T rho v v T	v
	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

Detailed Description

Common class for single phase fluid properties.

Definition at line 52 of file SinglePhaseFluidProperties.h.

Constructor & Destructor Documentation

SinglePhaseFluidProperties()

SinglePhaseFluidProperties::SinglePhaseFluidProperties

(

const InputParameters &

parameters

)

Definition at line 24 of file SinglePhaseFluidProperties.C.

  : FluidProperties(parameters),
    _R(8.3144598),
    _T_c2k(273.15),
    _allow_imperfect_jacobians(getParam<bool>("allow_imperfect_jacobians"))
{
}

~SinglePhaseFluidProperties()

SinglePhaseFluidProperties::~SinglePhaseFluidProperties ( )

virtual

Definition at line 32 of file SinglePhaseFluidProperties.C.

{}

Member Function Documentation

beta()

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

virtual

Definition at line 155 of file SinglePhaseFluidProperties.C.

Referenced by SimpleFluidProperties::beta_from_p_T(), and Water97FluidProperties::vaporTemperature().

{
  return beta_from_p_T(p, T);
}

beta_from_p_T() [1/2]

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

virtual

Reimplemented in SimpleFluidProperties.

Definition at line 86 of file SinglePhaseFluidProperties.C.

Referenced by beta().

{
  // The volumetric thermal expansion coefficient is defined as
  //   1/v dv/dT)_p
  // It is the fractional change rate of volume with respect to temperature change
  // at constant pressure. Here it is coded as
  //   - 1/rho drho/dT)_p
  // using chain rule with v = v(rho)

  Real rho, drho_dp, drho_dT;
  rho_from_p_T(p, T, rho, drho_dp, drho_dT);
  return -drho_dT / rho;
}

beta_from_p_T() [2/2]

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

virtual

Reimplemented in SimpleFluidProperties.

Definition at line 80 of file SinglePhaseFluidProperties.C.

{
  mooseError(name(), ": ", __PRETTY_FUNCTION__, " is not implemented.");
}

c()

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

virtual

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().

{
  mooseDeprecated(name(), ": c() is deprecated. Use c_from_p_T() instead");

  return c_from_p_T(p, T);
}

criticalDensity()

Real SinglePhaseFluidProperties::criticalDensity ( ) const

virtual

Critical density.

Returns

critical density (kg/m^3)

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

Definition at line 125 of file SinglePhaseFluidProperties.C.

Referenced by HelmholtzFluidProperties::c_from_p_T(), HelmholtzFluidProperties::cp_from_p_T(), HelmholtzFluidProperties::cv_from_p_T(), HelmholtzFluidProperties::e_from_p_T(), HelmholtzFluidProperties::h_from_p_T(), HelmholtzFluidProperties::p_from_rho_T(), IdealRealGasMixtureFluidProperties::p_T_from_v_e(), HelmholtzFluidProperties::rho_from_p_T(), HelmholtzFluidProperties::s_from_p_T(), and IdealRealGasMixtureFluidProperties::v_from_p_T().

{
  mooseError(name(), ": criticalDensity() is not implemented");
}

criticalInternalEnergy()

Real SinglePhaseFluidProperties::criticalInternalEnergy ( ) const

virtual

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().

{
  mooseError(name(), ": criticalInternalEnergy() is not implemented");
}

criticalPressure()

Real SinglePhaseFluidProperties::criticalPressure ( ) const

virtual

Critical pressure.

Returns

critical pressure (Pa)

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

Definition at line 113 of file SinglePhaseFluidProperties.C.

{
  mooseError(name(), ": criticalPressure() is not implemented");
}

criticalTemperature()

Real SinglePhaseFluidProperties::criticalTemperature ( ) const

virtual

Critical temperature.

Returns

critical temperature (K)

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

Definition at line 119 of file SinglePhaseFluidProperties.C.

Referenced by HelmholtzFluidProperties::c_from_p_T(), HelmholtzFluidProperties::cp_from_p_T(), HelmholtzFluidProperties::cv_from_p_T(), HelmholtzFluidProperties::e_from_p_T(), HelmholtzFluidProperties::h_from_p_T(), HelmholtzFluidProperties::p_from_rho_T(), HelmholtzFluidProperties::rho_from_p_T(), HelmholtzFluidProperties::s_from_p_T(), IdealRealGasMixtureFluidProperties::v_from_p_T(), and IdealRealGasMixtureFluidProperties::xs_prim_from_p_T().

{
  mooseError(name(), ": criticalTemperature() is not implemented");
}

e()

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

virtual

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(), 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(), 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(), rho_e_dpT(), rho_e_from_p_T(), StiffenedGasFluidProperties::s_from_T_v(), IdealGasFluidProperties::s_from_v_e(), StiffenedGasFluidProperties::s_from_v_e(), Water97FluidProperties::subregion3(), Water97FluidProperties::subregionVolume(), T_from_p_h(), IdealGasFluidProperties::T_from_v_e(), StiffenedGasFluidProperties::T_from_v_e(), StiffenedGasFluidProperties::v_e_spndl_from_T(), and Water97FluidProperties::vaporTemperature().

{
  mooseDeprecated(name(), ": e() is deprecated. Use e_from_p_T() instead");

  return e_from_p_T(p, T);
}

e_dpT()

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

virtual

Definition at line 300 of file SinglePhaseFluidProperties.C.

{
  mooseDeprecated(name(), ": e_dpT() is deprecated. Use e_from_p_T() instead");

  e_from_p_T(p, T, e, de_dp, de_dT);
}

e_from_p_T() [1/2]

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

virtual

Internal energy from pressure and temperature.

Parameters

[in]	p	pressure (Pa)
[in]	T	temperature (K)

Returns

internal energy (J/kg)

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

Definition at line 35 of file SinglePhaseFluidProperties.C.

Referenced by FluidPropertiesMaterialPT::computeQpProperties(), PorousFlowSingleComponentFluid::computeQpProperties(), GeneralVaporMixtureFluidProperties::cp_from_p_T(), GeneralVaporMixtureFluidProperties::cv_from_p_T(), e(), e_dpT(), GeneralVaporMixtureFluidProperties::e_from_p_T(), TabulatedFluidProperties::e_from_p_T(), TabulatedFluidProperties::generateTabulatedData(), PorousFlowSingleComponentFluid::initQpStatefulProperties(), GeneralVaporMixtureFluidProperties::k_from_p_T(), GeneralVaporMixtureFluidProperties::mu_from_p_T(), and rho_e_from_p_T().

{
  const Real rho = rho_from_p_T(p, T);
  return e_from_p_rho(p, rho);
}

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

virtual

Internal energy and its derivatives from pressure and temperature.

Parameters

[in]	p	pressure (Pa)
[in]	T	temperature (K)
[out]	e	internal energy (J/kg)
[out]	de_dp	derivative of internal energy w.r.t. pressure
[out]	de_dT	derivative 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.

{
  // From rho(p,T), compute: drho(p,T)/dp, drho(p,T)/dT
  Real rho = 0., drho_dp = 0., drho_dT = 0.;
  rho_from_p_T(p, T, rho, drho_dp, drho_dT);

  // From e(p, rho), compute: de(p,rho)/dp, de(p,rho)/drho
  Real depr_dp = 0., depr_drho = 0.;
  e_from_p_rho(p, rho, e, depr_dp, depr_drho);

  // Using partial derivative rules, we have:
  // de(p,T)/dp = de(p,rho)/dp * dp/dp + de(p,rho)/drho * drho(p,T)/dp, (dp/dp == 1)
  // de(p,T)/dT = de(p,rho)/dp * dp/dT + de(p,rho)/drho * drho(p,T)/dT, (dp/dT == 0)
  de_dp = depr_dp + depr_drho * drho_dp;
  de_dT = depr_drho * drho_dT;
}

e_spndl_from_v()

Real SinglePhaseFluidProperties::e_spndl_from_v ( Real  v ) const

virtual

Specific internal energy from temperature and specific volume.

Parameters

[in]	T	temperature
[in]	v	specific volume

Reimplemented in StiffenedGasFluidProperties.

Definition at line 452 of file SinglePhaseFluidProperties.C.

Referenced by IdealRealGasMixtureFluidProperties::p_T_from_v_e().

{
  mooseError(name(), ": ", __PRETTY_FUNCTION__, " not implemented.");
}

execute()

virtual void FluidProperties::execute ( )

inlinefinalvirtualinherited

Definition at line 27 of file FluidProperties.h.

{}

finalize()

virtual void FluidProperties::finalize ( )

inlinefinalvirtualinherited

Definition at line 29 of file FluidProperties.h.

{}

fluidName()

std::string SinglePhaseFluidProperties::fluidName ( ) const

virtual

Fluid name.

Returns

string representing fluid name

Reimplemented in TabulatedFluidProperties, CO2FluidProperties, NaClFluidProperties, Water97FluidProperties, HydrogenFluidProperties, NitrogenFluidProperties, SimpleFluidProperties, MethaneFluidProperties, and IdealGasFluidPropertiesPT.

Definition at line 107 of file SinglePhaseFluidProperties.C.

Referenced by TabulatedFluidProperties::fluidName(), PorousFlowBrineCO2::PorousFlowBrineCO2(), PorousFlowWaterNCG::PorousFlowWaterNCG(), and TabulatedFluidProperties::writeTabulatedData().

{
  return std::string("");
}

fluidPropError()

template<typename... Args>

void SinglePhaseFluidProperties::fluidPropError ( Args...  args ) const

inlineprivate

Definition at line 512 of file SinglePhaseFluidProperties.h.

  {
    if (_allow_imperfect_jacobians)
      mooseWarning(std::forward<Args>(args)...);
    else
      mooseError(std::forward<Args>(args)...);
  }

gamma_from_p_T()

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

virtual

Adiabatic index - ratio of specific heats.

Parameters

pressure	fluid pressure (Pa)
temperature	fluid temperature (K)

Returns

gamma (-)

Definition at line 149 of file SinglePhaseFluidProperties.C.

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

h()

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

virtual

Specific enthalpy from pressure and temperature.

Parameters

[in]	p	pressure (Pa)
[in]	T	temperature (K)

Returns

h (J/kg)

Definition at line 429 of file SinglePhaseFluidProperties.C.

Referenced by NaClFluidProperties::e_from_p_T(), IdealGasFluidProperties::e_from_v_h(), StiffenedGasFluidProperties::e_from_v_h(), h_dpT(), HelmholtzFluidProperties::h_from_p_T(), IdealGasFluidProperties::h_from_p_T(), StiffenedGasFluidProperties::h_from_p_T(), NaClFluidProperties::h_from_p_T(), IdealGasFluidPropertiesPT::h_from_p_T(), SimpleFluidProperties::h_from_p_T(), TabulatedFluidProperties::h_from_p_T(), Water97FluidProperties::h_from_p_T(), StiffenedGasFluidProperties::h_from_T_v(), IdealGasFluidProperties::h_from_T_v(), IdealGasFluidProperties::p_from_h_s(), StiffenedGasFluidProperties::p_from_h_s(), StiffenedGasFluidProperties::s_from_h_p(), IdealGasFluidProperties::s_from_h_p(), IdealGasFluidProperties::T_from_p_h(), and T_from_p_h().

{
  mooseDeprecated(name(), ": h() is deprecated. Use h_from_p_T() instead");

  return h_from_p_T(p, T);
}

h_dpT()

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

virtual

Specific enthalpy and its derivatives from pressure and temperature.

Parameters

[in]	p	pressure (Pa)
[in]	T	temperature (K)
[out]	h	specific enthalpy (J/kg)
[out]	dh_dp	derivative of specific enthalpy w.r.t. pressure
[out]	dh_dT	derivative of specific enthalpy w.r.t. temperature

Definition at line 437 of file SinglePhaseFluidProperties.C.

{
  mooseDeprecated(name(), ": h_dpT() is deprecated. Use h_from_p_T() instead");

  h_from_p_T(p, T, h, dh_dp, dh_dT);
}

henryConstant() [1/2]

Real SinglePhaseFluidProperties::henryConstant ( Real  temperature ) const

virtual

Henry's law constant for dissolution in water.

Parameters

temperature

fluid 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 henryConstant_dT().

{
  mooseError(name(), ": henryConstant() is not implemented");
}

henryConstant() [2/2]

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

virtual

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

Parameters

	temperature	fluid temperature (K)
[out]	Kh	Henry's constant
[out]	dKh_dT	derivative of Kh wrt temperature

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

Definition at line 250 of file SinglePhaseFluidProperties.C.

{
  mooseError(name(), ": henryConstant() is not implemented");
}

henryConstant_dT()

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

virtual

Definition at line 256 of file SinglePhaseFluidProperties.C.

{
  mooseDeprecated(name(), ": henryConstant_dT() is deprecated. Use henryConstant() instead");

  henryConstant(T, Kh, dKh_dT);
}

henryConstantIAPWS() [1/2]

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

protectedvirtual

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 henryConstantIAPWS_dT().

{
  const Real Tr = T / 647.096;
  const Real tau = 1.0 - Tr;

  const Real lnkh =
      A / Tr + B * std::pow(tau, 0.355) / Tr + C * std::pow(Tr, -0.41) * std::exp(tau);

  // The vapor pressure used in this formulation
  const std::vector<Real> a{
      -7.85951783, 1.84408259, -11.7866497, 22.6807411, -15.9618719, 1.80122502};
  const std::vector<Real> b{1.0, 1.5, 3.0, 3.5, 4.0, 7.5};
  Real sum = 0.0;

  for (std::size_t i = 0; i < a.size(); ++i)
    sum += a[i] * std::pow(tau, b[i]);

  return 22.064e6 * std::exp(sum / Tr) * std::exp(lnkh);
}

henryConstantIAPWS() [2/2]

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

protectedvirtual

Definition at line 182 of file SinglePhaseFluidProperties.C.

{
  const Real pc = 22.064e6;
  const Real Tc = 647.096;

  const Real Tr = T / Tc;
  const Real tau = 1.0 - Tr;

  const Real lnkh =
      A / Tr + B * std::pow(tau, 0.355) / Tr + C * std::pow(Tr, -0.41) * std::exp(tau);
  const Real dlnkh_dT =
      (-A / Tr / Tr - B * std::pow(tau, 0.355) / Tr / Tr - 0.355 * B * std::pow(tau, -0.645) / Tr -
       0.41 * C * std::pow(Tr, -1.41) * std::exp(tau) - C * std::pow(Tr, -0.41) * std::exp(tau)) /
      Tc;

  // The vapor pressure used in this formulation
  const std::vector<Real> a{
      -7.85951783, 1.84408259, -11.7866497, 22.6807411, -15.9618719, 1.80122502};
  const std::vector<Real> b{1.0, 1.5, 3.0, 3.5, 4.0, 7.5};
  Real sum = 0.0;
  Real dsum = 0.0;

  for (std::size_t i = 0; i < a.size(); ++i)
  {
    sum += a[i] * std::pow(tau, b[i]);
    dsum += a[i] * b[i] * std::pow(tau, b[i] - 1.0);
  }

  const Real p = pc * std::exp(sum / Tr);
  const Real dp_dT = -p / Tc / Tr * (sum / Tr + dsum);

  // Henry's constant and its derivative wrt temperature
  Kh = p * std::exp(lnkh);
  dKh_dT = (p * dlnkh_dT + dp_dT) * std::exp(lnkh);
}

henryConstantIAPWS_dT()

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

protectedvirtual

Definition at line 220 of file SinglePhaseFluidProperties.C.

{
  mooseDeprecated(name(),
                  ":henryConstantIAPWS_dT() is deprecated. Use henryConstantIAPWS() instead");

  henryConstantIAPWS(T, Kh, dKh_dT, A, B, C);
}

initialize()

virtual void FluidProperties::initialize ( )

inlinefinalvirtualinherited

Definition at line 28 of file FluidProperties.h.

{}

k()

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

virtual

Thermal conductivity.

Parameters

pressure	fluid pressure (Pa)
temperature	fluid temperature (K)

Returns

thermal conductivity (W/m/K)

Definition at line 405 of file SinglePhaseFluidProperties.C.

Referenced by k_dpT(), IdealGasFluidPropertiesPT::k_from_p_T(), MethaneFluidProperties::k_from_p_T(), SimpleFluidProperties::k_from_p_T(), NitrogenFluidProperties::k_from_p_T(), HydrogenFluidProperties::k_from_p_T(), NaClFluidProperties::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().

{
  mooseDeprecated(name(), ": k() is deprecated. Use k_from_p_T() instead");

  return k_from_p_T(p, T);
}

k_dpT()

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

virtual

Thermal conductivity and its derivatives wrt pressure and temperature.

Parameters

	pressure	fluid pressure (Pa)
	temperature	fluid temperature (K)
[out]	thermal	conductivity (W/m/K)
[out]	derivative	of thermal conductivity wrt pressure
[out]	derivative	of thermal conductivity wrt temperature

Definition at line 413 of file SinglePhaseFluidProperties.C.

{
  mooseDeprecated(name(), ": k_dpT() is deprecated. Use k_from_p_T() instead");

  k_from_p_T(p, T, k, dk_dp, dk_dT);
}

molarMass()

Real SinglePhaseFluidProperties::molarMass ( ) const

virtual

Molar mass [kg/mol].

Returns

molar mass

Reimplemented in TabulatedFluidProperties, CO2FluidProperties, StiffenedGasFluidProperties, IdealGasFluidProperties, NaClFluidProperties, Water97FluidProperties, HydrogenFluidProperties, SimpleFluidProperties, NitrogenFluidProperties, MethaneFluidProperties, and IdealGasFluidPropertiesPT.

Definition at line 101 of file SinglePhaseFluidProperties.C.

Referenced by BrineFluidProperties::BrineFluidProperties(), HelmholtzFluidProperties::c_from_p_T(), HelmholtzFluidProperties::cp_from_p_T(), HelmholtzFluidProperties::cv_from_p_T(), HelmholtzFluidProperties::e_from_p_T(), HelmholtzFluidProperties::h_from_p_T(), GeneralVaporMixtureFluidProperties::k_from_p_T(), IdealRealGasMixtureFluidProperties::k_from_p_T(), IdealRealGasMixtureFluidProperties::k_from_T_v(), TabulatedFluidProperties::molarMass(), GeneralVaporMixtureFluidProperties::mu_from_p_T(), IdealRealGasMixtureFluidProperties::mu_from_p_T(), IdealRealGasMixtureFluidProperties::mu_from_T_v(), HelmholtzFluidProperties::p_from_rho_T(), HelmholtzFluidProperties::rho_from_p_T(), HelmholtzFluidProperties::s_from_p_T(), and IdealRealGasMixtureFluidProperties::v_from_p_T().

{
  mooseError(name(), ": molarMass is not implemented");
}

mu()

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

virtual

Dynamic viscosity.

Parameters

pressure	fluid pressure (Pa)
temperature	fluid temperature (K)

Returns

viscosity (Pa.s)

Definition at line 345 of file SinglePhaseFluidProperties.C.

Referenced by mu_dpT(), 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(), rho_mu(), 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 rho_mu_from_p_T().

{
  mooseDeprecated(name(), ": mu() is deprecated. Use mu_from_p_T() instead");

  return mu_from_p_T(p, T);
}

mu_dpT()

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

virtual

Dynamic viscosity and its derivatives wrt pressure and temperature.

Parameters

	pressure	fluid pressure (Pa)
	temperature	fluid temperature (K)
[out]	mu	viscosity (Pa.s)
[out]	dmu_dp	derivative of viscosity wrt pressure
[out]	dmu_dT	derivative of viscosity wrt temperature

Definition at line 353 of file SinglePhaseFluidProperties.C.

{
  mooseDeprecated(name(), ": mu_dpT() is deprecated. Use mu_from_p_T() instead");

  mu_from_p_T(p, T, mu, dmu_dp, dmu_dT);
}

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

virtual

Definition at line 236 of file SinglePhaseFluidProperties.C.

{
  mooseDeprecated(name(), ":mu_drhoT_from_rho_T() is deprecated. Use mu_from_rho_T() instead");

  mu_from_rho_T(rho, T, drho_dT, mu, dmu_drho, dmu_dT);
}

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

virtual

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

	density	fluid density (kg/m^3)
	temperature	fluid temperature (K)
	ddensity_dT	derivative of density wrt temperature
[out]	mu	viscosity (Pa.s)
[out]	dmu_drho	derivative of viscosity wrt density
[out]	dmu_dT	derivative of viscosity wrt temperature

Reimplemented in Water97FluidProperties, CO2FluidProperties, HydrogenFluidProperties, and NitrogenFluidProperties.

Definition at line 230 of file SinglePhaseFluidProperties.C.

Referenced by mu_drhoT_from_rho_T().

{
  mooseError(name(), ": mu_from_rho_T is not implemented.");
}

propfunc() [1/15]

SinglePhaseFluidProperties::propfunc	(	p	,
		v	,
		e
	)

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
	)

propfunc() [3/15]

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

propfunc() [4/15]

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

propfunc() [5/15]

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

propfunc() [6/15]

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

propfunc() [7/15]

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

propfunc() [8/15]

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

propfunc() [9/15]

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

propfunc() [10/15]

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

propfunc() [11/15]

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

propfunc() [12/15]

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

propfunc() [13/15]

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

propfunc() [14/15]

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

propfunc() [15/15]

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

rho()

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

virtual

Density from pressure and temperature.

Parameters

[in]	p	pressure (Pa)
[in]	T	temperature (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

virtual

Density and its derivatives from pressure and temperature.

Parameters

[in]	p	pressure (Pa)
[in]	T	temperature (K)
[out]	rho	density (kg/m^3)
[out]	drho_dp	derivative of density w.r.t. pressure
[out]	drho_dT	derivative of density w.r.t. temperature

Definition at line 283 of file SinglePhaseFluidProperties.C.

{
  mooseDeprecated(name(), ": rho_dpT() is deprecated. Use rho_from_p_T() instead");

  rho_from_p_T(p, T, rho, drho_dp, drho_dT);
}

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

virtual

Reimplemented in IdealGasFluidPropertiesPT.

Definition at line 322 of file SinglePhaseFluidProperties.C.

{
  mooseDeprecated(name(), ": rho_e_dpT() is deprecated. Use rho_e_from_p_T() instead");

  rho_e_from_p_T(p, T, rho, drho_dp, drho_dT, e, de_dp, de_dT);
}

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

virtual

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

Parameters

	pressure	fluid pressure (Pa)
	temperature	fluid temperature (K)
[out]	rho	density (kg/m^3)
[out]	drho_dp	derivative of density wrt pressure
[out]	drho_dT	derivative of density wrt temperature
[out]	e	internal energy (J/kg)
[out]	de_dp	derivative of internal energy wrt pressure
[out]	de_dT	derivative of internal energy wrt temperature

Definition at line 308 of file SinglePhaseFluidProperties.C.

Referenced by rho_e_dpT().

{
  rho_from_p_T(p, T, rho, drho_dp, drho_dT);
  e_from_p_T(p, T, e, de_dp, de_dT);
}

rho_mu()

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

virtual

Density and viscosity.

Parameters

	pressure	fluid pressure (Pa)
	temperature	fluid temperature (K)
[out]	rho	density (kg/m^3)
[out]	mu	viscosity (Pa.s)

Definition at line 361 of file SinglePhaseFluidProperties.C.

{
  mooseDeprecated(name(), ": rho_mu() is deprecated. Use rho_mu_from_p_T() instead");

  rho_mu_from_p_T(p, T, rho, mu);
}

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

virtual

Definition at line 376 of file SinglePhaseFluidProperties.C.

{
  mooseDeprecated(name(), ": rho_mu_dpT() is deprecated. Use rho_mu_from_p_T() instead");

  rho_mu_from_p_T(p, T, rho, drho_dp, drho_dT, mu, dmu_dp, dmu_dT);
}

rho_mu_from_p_T() [1/2]

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

virtual

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

Definition at line 369 of file SinglePhaseFluidProperties.C.

Referenced by PorousFlowSingleComponentFluid::computeQpProperties(), PorousFlowWaterNCG::gasProperties(), PorousFlowBrineCO2::gasProperties(), PorousFlowWaterNCG::liquidProperties(), rho_mu(), and rho_mu_dpT().

{
  rho = rho_from_p_T(p, T);
  mu = mu_from_p_T(p, T);
}

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

virtual

Density and viscosity and their derivatives wrt pressure and temperature.

Parameters

	pressure	fluid pressure (Pa)
	temperature	fluid temperature (K)
[out]	rho	density (kg/m^3)
[out]	drho_dp	derivative of density wrt pressure
[out]	drho_dT	derivative of density wrt temperature
[out]	mu	viscosity (Pa.s)
[out]	dmu_dp	derivative of viscosity wrt pressure
[out]	dmu_dT	derivative of viscosity wrt temperature

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

Definition at line 391 of file SinglePhaseFluidProperties.C.

{
  rho_from_p_T(p, T, rho, drho_dp, drho_dT);
  mu_from_p_T(p, T, mu, dmu_dp, dmu_dT);
}

s()

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

virtual

Definition at line 421 of file SinglePhaseFluidProperties.C.

Referenced by IdealGasFluidProperties::p_from_h_s(), StiffenedGasFluidProperties::p_from_h_s(), IdealGasFluidProperties::rho_from_p_s(), StiffenedGasFluidProperties::rho_from_p_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(), HelmholtzFluidProperties::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(), IdealGasFluidProperties::s_from_v_e(), StiffenedGasFluidProperties::s_from_v_e(), and T_from_p_h().

{
  mooseDeprecated(name(), ": s() is deprecated. Use s_from_p_T() instead");

  return s_from_p_T(p, T);
}

subdomainSetup()

virtual void FluidProperties::subdomainSetup ( )

inlinefinalvirtualinherited

Definition at line 32 of file FluidProperties.h.

{}

T_from_p_h()

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

virtual

Temperature from pressure and specific enthalpy.

Parameters

[in]	pressure	pressure (Pa)
[in]	enthalpy	enthalpy (J/kg)

Returns

Temperature (K)

Reimplemented in IdealGasFluidProperties.

Definition at line 464 of file SinglePhaseFluidProperties.C.

{
  const Real s = s_from_h_p(h, p);
  const Real rho = rho_from_p_s(p, s);
  const Real v = 1. / rho;
  const Real e = e_from_v_h(v, h);
  return T_from_v_e(v, e);
}

threadJoin()

virtual void FluidProperties::threadJoin ( const UserObject &  )

inlinefinalvirtualinherited

Definition at line 31 of file FluidProperties.h.

{}

triplePointPressure()

Real SinglePhaseFluidProperties::triplePointPressure ( ) const

virtual

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.

{
  mooseError(name(), ": triplePointPressure() is not implemented");
}

triplePointTemperature()

Real SinglePhaseFluidProperties::triplePointTemperature ( ) const

virtual

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.

{
  mooseError(name(), ": triplePointTemperature() is not implemented");
}

v_e_spndl_from_T()

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

virtual

Specific internal energy from temperature and specific volume.

Parameters

[in]	T	temperature
[in]	v	specific volume

Reimplemented in StiffenedGasFluidProperties.

Definition at line 458 of file SinglePhaseFluidProperties.C.

Referenced by IdealRealGasMixtureFluidProperties::v_from_p_T().

{
  mooseError(name(), ": ", __PRETTY_FUNCTION__, " not implemented.");
}

v_from_p_T() [1/2]

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

virtual

Specific volume from pressure and temperature.

Parameters

[in]	p	pressure
[in]	T	temperature

Definition at line 60 of file SinglePhaseFluidProperties.C.

Referenced by GeneralVaporMixtureFluidProperties::c_from_p_T(), GeneralVaporMixtureFluidProperties::cp_from_p_T(), GeneralVaporMixtureFluidProperties::cv_from_p_T(), GeneralVaporMixtureFluidProperties::k_from_p_T(), GeneralVaporMixtureFluidProperties::mu_from_p_T(), GeneralVaporMixtureFluidProperties::v_from_p_T(), and IdealRealGasMixtureFluidProperties::xs_prim_from_p_T().

{
  const Real rho = rho_from_p_T(p, T);
  return 1.0 / rho;
}

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

virtual

Specific volume and its derivatives from pressure and temperature.

Parameters

[in]	p	pressure
[in]	T	temperature
[out]	v	specific volume
[out]	dv_dp	derivative of specific volume w.r.t. pressure
[out]	dv_dT	derivative of specific volume w.r.t. temperature

Definition at line 67 of file SinglePhaseFluidProperties.C.

{
  Real rho, drho_dp, drho_dT;
  rho_from_p_T(p, T, rho, drho_dp, drho_dT);

  v = 1.0 / rho;
  const Real dv_drho = -1.0 / (rho * rho);

  dv_dp = dv_drho * drho_dp;
  dv_dT = dv_drho * drho_dT;
}

vaporPressure() [1/2]

Real SinglePhaseFluidProperties::vaporPressure ( Real  temperature ) const

virtual

Vapor pressure.

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

Parameters

temperature

water 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 vaporPressure_dT().

{
  mooseError(name(), ": vaporPressure() is not implemented");
}

vaporPressure() [2/2]

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

virtual

Vapor pressure.

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

Parameters

	temperature	water temperature (K)
[out]	saturation	pressure (Pa)
[out]	derivative	of saturation pressure wrt temperature (Pa/K)

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

Definition at line 269 of file SinglePhaseFluidProperties.C.

{
  mooseError(name(), ": vaporPressure() is not implemented");
}

vaporPressure_dT()

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

virtual

Definition at line 275 of file SinglePhaseFluidProperties.C.

{
  mooseDeprecated(name(), ": vaporPressure_dT() is deprecated. Use vaporPressure() instead");

  vaporPressure(T, psat, dpsat_dT);
}

Member Data Documentation

_allow_imperfect_jacobians

bool SinglePhaseFluidProperties::_allow_imperfect_jacobians

private

Definition at line 519 of file SinglePhaseFluidProperties.h.

Referenced by fluidPropError().

_R

const Real SinglePhaseFluidProperties::_R

protected

Universal gas constant (J/mol/K)

Definition at line 506 of file SinglePhaseFluidProperties.h.

Referenced by IdealGasFluidPropertiesPT::c_from_p_T(), HelmholtzFluidProperties::c_from_p_T(), HelmholtzFluidProperties::cp_from_p_T(), HelmholtzFluidProperties::cv_from_p_T(), HelmholtzFluidProperties::e_from_p_T(), HelmholtzFluidProperties::h_from_p_T(), HelmholtzFluidProperties::p_from_rho_T(), HelmholtzFluidProperties::rho_from_p_T(), IdealGasFluidPropertiesPT::rho_from_p_T(), and HelmholtzFluidProperties::s_from_p_T().

_T_c2k

const Real SinglePhaseFluidProperties::_T_c2k

protected

Conversion of temperature from Celsius to Kelvin.

Definition at line 508 of file SinglePhaseFluidProperties.h.

Referenced by NaClFluidProperties::cp_from_p_T(), NaClFluidProperties::h_from_p_T(), NaClFluidProperties::k_from_p_T(), CO2FluidProperties::partialDensity(), and NaClFluidProperties::rho_from_p_T().

p [1/7]

e e e e SinglePhaseFluidProperties::p

Definition at line 130 of file SinglePhaseFluidProperties.h.

Referenced by beta(), beta_from_p_T(), c(), StiffenedGasFluidProperties::c_from_v_e(), e(), e_dpT(), StiffenedGasFluidProperties::e_from_p_rho(), IdealGasFluidProperties::e_from_p_rho(), IdealGasFluidProperties::e_from_p_T(), StiffenedGasFluidProperties::e_from_p_T(), e_from_p_T(), IdealGasFluidProperties::g_from_v_e(), StiffenedGasFluidProperties::g_from_v_e(), gamma_from_p_T(), TabulatedFluidProperties::generateTabulatedData(), h(), h_dpT(), IdealGasFluidProperties::h_from_p_T(), StiffenedGasFluidProperties::h_from_p_T(), henryConstantIAPWS(), k(), k_dpT(), mu(), 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(), rho_dpT(), rho_e_dpT(), 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(), rho_mu(), rho_mu_dpT(), rho_mu_from_p_T(), 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(), IdealGasFluidProperties::s_from_v_e(), StiffenedGasFluidProperties::s_from_v_e(), T_from_p_h(), v_from_p_T(), Water97FluidProperties::vaporPressure(), and TabulatedFluidProperties::writeTabulatedData().

p [2/7]

e e e e s SinglePhaseFluidProperties::p

Definition at line 132 of file SinglePhaseFluidProperties.h.

p [3/7]

e e e e s T T SinglePhaseFluidProperties::p

Definition at line 136 of file SinglePhaseFluidProperties.h.

p [4/7]

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

Definition at line 138 of file SinglePhaseFluidProperties.h.

p [5/7]

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

Definition at line 140 of file SinglePhaseFluidProperties.h.

p [6/7]

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

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

Definition at line 148 of file SinglePhaseFluidProperties.h.

rho

Real SinglePhaseFluidProperties::rho

Definition at line 134 of file SinglePhaseFluidProperties.h.

Referenced by beta_from_p_T(), StiffenedGasFluidProperties::c2_from_p_rho(), StiffenedGasFluidProperties::e_from_p_rho(), IdealGasFluidProperties::e_from_p_rho(), NaClFluidProperties::e_from_p_T(), e_from_p_T(), IdealGasFluidProperties::h_from_p_T(), Water97FluidProperties::k_from_p_T(), 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(), rho_dpT(), IdealGasFluidPropertiesPT::rho_e_dpT(), rho_e_dpT(), 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(), rho_mu(), 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(), rho_mu_from_p_T(), T_from_p_h(), and v_from_p_T().

T [1/2]

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

Definition at line 144 of file SinglePhaseFluidProperties.h.

Referenced by beta(), beta_from_p_T(), c(), IdealGasFluidProperties::c_from_v_e(), e(), e_dpT(), IdealGasFluidProperties::e_from_p_T(), StiffenedGasFluidProperties::e_from_p_T(), e_from_p_T(), StiffenedGasFluidProperties::e_from_T_v(), IdealGasFluidProperties::e_from_T_v(), IdealGasFluidProperties::g_from_v_e(), StiffenedGasFluidProperties::g_from_v_e(), gamma_from_p_T(), h(), h_dpT(), IdealGasFluidProperties::h_from_p_T(), StiffenedGasFluidProperties::h_from_p_T(), StiffenedGasFluidProperties::h_from_T_v(), IdealGasFluidProperties::h_from_T_v(), henryConstant_dT(), henryConstantIAPWS(), henryConstantIAPWS_dT(), k(), k_dpT(), mu(), mu_dpT(), mu_drhoT_from_rho_T(), StiffenedGasFluidProperties::p_from_T_v(), IdealGasFluidProperties::p_from_T_v(), rho_dpT(), rho_e_dpT(), 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(), rho_mu(), rho_mu_dpT(), rho_mu_from_p_T(), 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(), IdealGasFluidProperties::s_from_v_e(), StiffenedGasFluidProperties::s_from_v_e(), IdealGasFluidProperties::T_from_v_e(), StiffenedGasFluidProperties::T_from_v_e(), v_from_p_T(), and vaporPressure_dT().

T [2/2]

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

Definition at line 146 of file SinglePhaseFluidProperties.h.

v [1/5]

SinglePhaseFluidProperties::v

Definition at line 122 of file SinglePhaseFluidProperties.h.

Referenced by IdealGasFluidProperties::c_from_v_e(), StiffenedGasFluidProperties::c_from_v_e(), IdealGasFluidProperties::cp_from_v_e(), StiffenedGasFluidProperties::cp_from_v_e(), StiffenedGasFluidProperties::e_from_T_v(), IdealGasFluidProperties::e_from_v_h(), StiffenedGasFluidProperties::e_from_v_h(), IdealGasFluidProperties::g_from_v_e(), StiffenedGasFluidProperties::g_from_v_e(), StiffenedGasFluidProperties::p_from_T_v(), IdealGasFluidProperties::p_from_T_v(), IdealGasFluidProperties::p_from_v_e(), StiffenedGasFluidProperties::p_from_v_e(), StiffenedGasFluidProperties::s_from_T_v(), IdealGasFluidProperties::s_from_T_v(), StiffenedGasFluidProperties::s_from_v_e(), IdealGasFluidProperties::s_from_v_e(), T_from_p_h(), StiffenedGasFluidProperties::T_from_v_e(), IdealGasFluidProperties::T_from_v_e(), StiffenedGasFluidProperties::v_e_spndl_from_T(), and v_from_p_T().

v [2/5]

e SinglePhaseFluidProperties::v

Definition at line 124 of file SinglePhaseFluidProperties.h.

v [3/5]

e e SinglePhaseFluidProperties::v

Definition at line 126 of file SinglePhaseFluidProperties.h.

v [4/5]

e e e SinglePhaseFluidProperties::v

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

Definition at line 150 of file SinglePhaseFluidProperties.h.

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

• fluid_properties/include/userobjects/SinglePhaseFluidProperties.h
• fluid_properties/src/userobjects/SinglePhaseFluidProperties.C