IdealGasFluidProperties Class Reference

Ideal gas fluid properties. More...

#include <IdealGasFluidProperties.h>

Inheritance diagram for IdealGasFluidProperties:

Public Member Functions
	IdealGasFluidProperties (const InputParameters &parameters)
virtual	~IdealGasFluidProperties ()
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	T_from_v_e (Real v, Real e) const override
virtual void	T_from_v_e (Real v, Real e, Real &T, Real &dT_dv, Real &dT_de) const override
virtual Real	c_from_v_e (Real v, Real e) const override
virtual void	c_from_v_e (Real v, Real e, Real &c, Real &dc_dv, Real &dc_de) const override
virtual Real	cp_from_v_e (Real v, Real e) const override
virtual void	cp_from_v_e (Real v, Real e, Real &cp, Real &dcp_dv, Real &dcp_de) const override
virtual Real	cv_from_v_e (Real v, Real e) const override
virtual Real	mu_from_v_e (Real v, Real e) const override
virtual Real	k_from_v_e (Real v, Real e) const override
virtual Real	s_from_v_e (Real v, Real e) const override
virtual void	s_from_v_e (Real v, Real e, Real &s, Real &ds_dv, Real &ds_de) const override
virtual Real	s_from_p_T (Real p, Real T) const override
virtual void	s_from_p_T (Real p, Real T, Real &s, Real &ds_dp, Real &ds_dT) const override
virtual Real	s_from_h_p (Real h, Real p) const override
virtual void	s_from_h_p (Real h, Real p, Real &s, Real &ds_dh, Real &ds_dp) const override
virtual Real	rho_from_p_s (Real p, Real s) const override
virtual void	rho_from_p_s (Real p, Real s, Real &rho, Real &drho_dp, Real &drho_ds) const override
virtual Real	e_from_v_h (Real v, Real h) const override
virtual void	e_from_v_h (Real v, Real h, Real &e, Real &de_dv, Real &de_dh) const override
virtual Real	rho_from_p_T (Real p, Real T) const override
virtual void	rho_from_p_T (Real p, Real T, Real &rho, Real &drho_dp, Real &drho_dT) const override
virtual Real	e_from_p_rho (Real p, Real rho) const override
virtual void	e_from_p_rho (Real p, Real rho, Real &e, Real &de_dp, Real &de_drho) const override
virtual Real	e_from_T_v (Real T, Real v) const override
virtual void	e_from_T_v (Real T, Real v, Real &e, Real &de_dT, Real &de_dv) const override
virtual Real	p_from_T_v (Real T, Real v) const override
virtual void	p_from_T_v (Real T, Real v, Real &p, Real &dp_dT, Real &dp_dv) const override
virtual Real	h_from_T_v (Real T, Real v) const override
virtual void	h_from_T_v (Real T, Real v, Real &h, Real &dh_dT, Real &dh_dv) const override
virtual Real	s_from_T_v (Real T, Real v) const override
virtual void	s_from_T_v (Real T, Real v, Real &s, Real &ds_dT, Real &ds_dv) const override
virtual Real	cv_from_T_v (Real T, Real v) const override
virtual Real	h_from_p_T (Real p, Real T) const override
virtual void	h_from_p_T (Real p, Real T, Real &h, Real &dh_dp, Real &dh_dT) const override
virtual Real	e_from_p_T (Real p, Real T) const override
	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 override
	Internal energy and its derivatives from pressure and temperature. More...
virtual Real	p_from_h_s (Real h, Real s) const override
virtual void	p_from_h_s (Real h, Real s, Real &p, Real &dp_dh, Real &dp_ds) const override
virtual Real	g_from_v_e (Real v, Real e) const override
virtual Real	T_from_p_h (Real p, Real h) const override
	Temperature from pressure and specific enthalpy. More...
virtual Real	molarMass () const override
	Molar mass [kg/mol]. More...
virtual Real	cv_from_p_T (Real p, Real T) const override
virtual Real	cp_from_p_T (Real p, Real T) const override
virtual void	cp_from_p_T (Real p, Real T, Real &cp, Real &dcp_dp, Real &dcp_dT) const override
virtual Real	mu_from_p_T (Real p, Real T) const override
virtual void	mu_from_p_T (Real p, Real T, Real &mu, Real &dmu_dp, Real &dmu_dT) const override
virtual Real	k_from_p_T (Real pressure, Real temperature) const override
virtual void	k_from_p_T (Real pressure, Real temperature, Real &k, Real &dk_dp, Real &dk_dT) const override
virtual Real	gamma () const
virtual Real	cv () const
virtual Real	cp () const
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 (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	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
Real	_gamma
Real	_R
Real	_cv
Real	_cp
Real	_mu
Real	_k
const Real	_T_c2k
	Conversion of temperature from Celsius to Kelvin. More...

Static Protected Attributes
static constexpr Real	R_universal = 8.3144598
	Universal gas constant [J/K.mol]. 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

Ideal gas fluid properties.

Definition at line 26 of file IdealGasFluidProperties.h.

Constructor & Destructor Documentation

IdealGasFluidProperties()

IdealGasFluidProperties::IdealGasFluidProperties

(

const InputParameters &

parameters

)

Definition at line 28 of file IdealGasFluidProperties.C.

  : SinglePhaseFluidProperties(parameters),
    _gamma(getParam<Real>("gamma")),
    _R(getParam<Real>("R")),
    _mu(getParam<Real>("mu")),
    _k(getParam<Real>("k"))
{
  _cp = _gamma * _R / (_gamma - 1.0);
  _cv = _cp / _gamma;
}

~IdealGasFluidProperties()

IdealGasFluidProperties::~IdealGasFluidProperties ( )

virtual

Definition at line 39 of file IdealGasFluidProperties.C.

{}

Member Function Documentation

beta()

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

virtualinherited

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

virtualinherited

Reimplemented in SimpleFluidProperties.

Definition at line 86 of file SinglePhaseFluidProperties.C.

Referenced by SinglePhaseFluidProperties::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

virtualinherited

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

virtualinherited

Definition at line 337 of file SinglePhaseFluidProperties.C.

Referenced by 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);
}

c_from_v_e() [1/2]

Real IdealGasFluidProperties::c_from_v_e ( Real  v, Real  e  ) const

overridevirtual

Definition at line 74 of file IdealGasFluidProperties.C.

Referenced by NSInitialCondition::value().

{
  Real T = T_from_v_e(v, e);

  const Real c2 = _gamma * _R * T;
  if (c2 < 0)
    mooseException(name() + ": Sound speed squared (gamma * R * T) is negative: c2 = " +
                   Moose::stringify(c2) + ".");

  return std::sqrt(c2);
}

c_from_v_e() [2/2]

void IdealGasFluidProperties::c_from_v_e ( Real  v, Real  e, Real &  c, Real &  dc_dv, Real &  dc_de  ) const

overridevirtual

Definition at line 87 of file IdealGasFluidProperties.C.

{
  Real T, dT_dv, dT_de;
  T_from_v_e(v, e, T, dT_dv, dT_de);

  c = std::sqrt(_gamma * _R * T);

  const Real dc_dT = 0.5 / c * _gamma * _R;
  dc_dv = dc_dT * dT_dv;
  dc_de = dc_dT * dT_de;
}

cp()

Real IdealGasFluidProperties::cp ( ) const

virtual

Definition at line 110 of file IdealGasFluidProperties.C.

Referenced by NavierStokesMaterial::computeProperties(), NavierStokesMaterial::computeTau(), cp_from_p_T(), cp_from_v_e(), and NSWeakStagnationBaseBC::staticValues().

{
  return _cp;
}

cp_from_p_T() [1/2]

Real IdealGasFluidProperties::cp_from_p_T ( Real  p, Real  T  ) const

overridevirtual

Definition at line 442 of file IdealGasFluidProperties.C.

Referenced by cp_from_p_T().

{
  return _cp;
}

cp_from_p_T() [2/2]

void IdealGasFluidProperties::cp_from_p_T ( Real  p, Real  T, Real &  cp, Real &  dcp_dp, Real &  dcp_dT  ) const

overridevirtual

Definition at line 448 of file IdealGasFluidProperties.C.

{
  cp = cp_from_p_T(pressure, temperature);
  dcp_dp = 0.0;
  dcp_dT = 0.0;
}

cp_from_v_e() [1/2]

Real IdealGasFluidProperties::cp_from_v_e ( Real  v, Real  e  ) const

overridevirtual

Definition at line 99 of file IdealGasFluidProperties.C.

Referenced by cp_from_v_e().

{ return _cp; }

cp_from_v_e() [2/2]

void IdealGasFluidProperties::cp_from_v_e ( Real  v, Real  e, Real &  cp, Real &  dcp_dv, Real &  dcp_de  ) const

overridevirtual

Definition at line 102 of file IdealGasFluidProperties.C.

{
  cp = cp_from_v_e(v, e);
  dcp_dv = 0.0;
  dcp_de = 0.0;
}

criticalDensity()

Real SinglePhaseFluidProperties::criticalDensity ( ) const

virtualinherited

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

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().

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

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.

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

criticalTemperature()

Real SinglePhaseFluidProperties::criticalTemperature ( ) const

virtualinherited

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");
}

cv()

Real IdealGasFluidProperties::cv ( ) const

virtual

Definition at line 118 of file IdealGasFluidProperties.C.

Referenced by NSEnergyWeakStagnationBC::computeQpResidual(), NSThermalBC::computeQpResidual(), NSInflowThermalBC::computeQpResidual(), NSEnergyInviscidBC::qpResidualHelper(), and NSInitialCondition::value().

{
  return _cv;
}

cv_from_p_T()

Real IdealGasFluidProperties::cv_from_p_T ( Real  p, Real  T  ) const

overridevirtual

Definition at line 437 of file IdealGasFluidProperties.C.

{
  return _cv;
}

cv_from_T_v()

Real IdealGasFluidProperties::cv_from_T_v ( Real  T, Real  v  ) const

overridevirtual

Definition at line 358 of file IdealGasFluidProperties.C.

{ return _cv; }

cv_from_v_e()

Real IdealGasFluidProperties::cv_from_v_e ( Real  v, Real  e  ) const

overridevirtual

Definition at line 115 of file IdealGasFluidProperties.C.

{ return _cv; }

e()

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

virtualinherited

Definition at line 292 of file SinglePhaseFluidProperties.C.

Referenced by Water97FluidProperties::b2bc(), c_from_v_e(), StiffenedGasFluidProperties::c_from_v_e(), NaClFluidProperties::cp_from_p_T(), cp_from_v_e(), StiffenedGasFluidProperties::cp_from_v_e(), Water97FluidProperties::densityRegion3(), SinglePhaseFluidProperties::e_dpT(), StiffenedGasFluidProperties::e_from_p_rho(), e_from_p_rho(), HelmholtzFluidProperties::e_from_p_T(), IdealGasFluidPropertiesPT::e_from_p_T(), Water97FluidProperties::e_from_p_T(), NaClFluidProperties::e_from_p_T(), 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(), e_from_T_v(), e_from_v_h(), StiffenedGasFluidProperties::e_from_v_h(), g_from_v_e(), StiffenedGasFluidProperties::g_from_v_e(), 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(), 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(), s_from_v_e(), StiffenedGasFluidProperties::s_from_v_e(), Water97FluidProperties::subregion3(), Water97FluidProperties::subregionVolume(), SinglePhaseFluidProperties::T_from_p_h(), 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

virtualinherited

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_rho() [1/2]

Real IdealGasFluidProperties::e_from_p_rho ( Real  p, Real  rho  ) const

overridevirtual

Definition at line 284 of file IdealGasFluidProperties.C.

Referenced by e_from_p_rho().

{
  return p / (_gamma - 1.0) / rho;
}

e_from_p_rho() [2/2]

void IdealGasFluidProperties::e_from_p_rho ( Real  p, Real  rho, Real &  e, Real &  de_dp, Real &  de_drho  ) const

overridevirtual

Definition at line 290 of file IdealGasFluidProperties.C.

{
  e = e_from_p_rho(p, rho);
  de_dp = 1.0 / (_gamma - 1.0) / rho;
  de_drho = -p / (_gamma - 1.0) / rho / rho;
}

e_from_p_T() [1/2]

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

overridevirtual

Internal energy from pressure and temperature.

Parameters

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

Returns

internal energy (J/kg)

Reimplemented from SinglePhaseFluidProperties.

Definition at line 378 of file IdealGasFluidProperties.C.

Referenced by e_from_p_T().

{
  return _cv * T;
}

e_from_p_T() [2/2]

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

overridevirtual

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 from SinglePhaseFluidProperties.

Definition at line 384 of file IdealGasFluidProperties.C.

{
  e = e_from_p_T(p, T);
  de_dp = 0.;
  de_dT = _cv;
}

e_from_T_v() [1/2]

Real IdealGasFluidProperties::e_from_T_v ( Real  T, Real  v  ) const

overridevirtual

Definition at line 299 of file IdealGasFluidProperties.C.

{
  return _cv * T;
}

e_from_T_v() [2/2]

void IdealGasFluidProperties::e_from_T_v ( Real  T, Real  v, Real &  e, Real &  de_dT, Real &  de_dv  ) const

overridevirtual

Definition at line 305 of file IdealGasFluidProperties.C.

{
  e = _cv * T;
  de_dT = _cv;
  de_dv = 0.0;
}

e_from_v_h() [1/2]

Real IdealGasFluidProperties::e_from_v_h ( Real  v, Real  h  ) const

overridevirtual

Definition at line 250 of file IdealGasFluidProperties.C.

Referenced by e_from_v_h().

{
  return h / _gamma;
}

e_from_v_h() [2/2]

void IdealGasFluidProperties::e_from_v_h ( Real  v, Real  h, Real &  e, Real &  de_dv, Real &  de_dh  ) const

overridevirtual

Definition at line 256 of file IdealGasFluidProperties.C.

{
  e = e_from_v_h(v, h);
  de_dv = 0.0;
  de_dh = 1.0 / _gamma;
}

e_spndl_from_v()

Real SinglePhaseFluidProperties::e_spndl_from_v ( Real  v ) const

virtualinherited

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

virtualinherited

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("");
}

g_from_v_e()

Real IdealGasFluidProperties::g_from_v_e ( Real  v, Real  e  ) const

overridevirtual

Definition at line 410 of file IdealGasFluidProperties.C.

{
  // g(p,T) for SGEOS is given by Equation (37) in the following reference:
  //
  // Ray A. Berry, Richard Saurel, Olivier LeMetayer
  // The discrete equation method (DEM) for fully compressible, two-phase flows in
  //   ducts of spatially varying cross-section
  // Nuclear Engineering and Design 240 (2010) p. 3797-3818
  //
  const Real p = p_from_v_e(v, e);
  const Real T = T_from_v_e(v, e);

  return _gamma * _cv * T - _cv * T * std::log(std::pow(T, _gamma) / std::pow(p, _gamma - 1.0));
}

gamma()

Real IdealGasFluidProperties::gamma ( ) const

virtual

Definition at line 124 of file IdealGasFluidProperties.C.

Referenced by NSSUPGEnergy::computeJacobianHelper(), NSSUPGMomentum::computeJacobianHelper(), NSMomentumInviscidFlux::computeJacobianHelper(), NSEntropyError::computeQpIntegral(), NSEnergyInviscidFlux::computeQpJacobian(), NSEnergyInviscidFlux::computeQpOffDiagJacobian(), NSSUPGEnergy::computeQpResidual(), NSSUPGMomentum::computeQpResidual(), NSStagnationTemperatureBC::computeQpResidual(), NSStagnationPressureBC::computeQpResidual(), NavierStokesMaterial::computeStrongResiduals(), NSEnergyInviscidBC::qpResidualHelper(), and NSWeakStagnationBaseBC::staticValues().

{
  return _gamma;
}

gamma_from_p_T()

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

virtualinherited

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

virtualinherited

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(), e_from_v_h(), StiffenedGasFluidProperties::e_from_v_h(), SinglePhaseFluidProperties::h_dpT(), HelmholtzFluidProperties::h_from_p_T(), 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(), h_from_T_v(), p_from_h_s(), StiffenedGasFluidProperties::p_from_h_s(), StiffenedGasFluidProperties::s_from_h_p(), s_from_h_p(), T_from_p_h(), and SinglePhaseFluidProperties::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

virtualinherited

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);
}

h_from_p_T() [1/2]

Real IdealGasFluidProperties::h_from_p_T ( Real  p, Real  T  ) const

overridevirtual

Definition at line 361 of file IdealGasFluidProperties.C.

Referenced by h_from_p_T().

{
  Real rho = rho_from_p_T(p, T);
  Real e = T * _cv;
  return e + p / rho;
}

h_from_p_T() [2/2]

void IdealGasFluidProperties::h_from_p_T ( Real  p, Real  T, Real &  h, Real &  dh_dp, Real &  dh_dT  ) const

overridevirtual

Definition at line 369 of file IdealGasFluidProperties.C.

{
  h = h_from_p_T(p, T);
  Real rho = rho_from_p_T(p, T);
  dh_dp = 0.0;
  dh_dT = _cv + p / rho / T;
}

h_from_T_v() [1/2]

Real IdealGasFluidProperties::h_from_T_v ( Real  T, Real  v  ) const

overridevirtual

Definition at line 327 of file IdealGasFluidProperties.C.

{
  return _gamma * _cv * T;
}

h_from_T_v() [2/2]

void IdealGasFluidProperties::h_from_T_v ( Real  T, Real  v, Real &  h, Real &  dh_dT, Real &  dh_dv  ) const

overridevirtual

Definition at line 333 of file IdealGasFluidProperties.C.

{
  h = _gamma * _cv * T;
  dh_dT = _gamma * _cv;
  dh_dv = 0.0;
}

henryConstant() [1/2]

Real SinglePhaseFluidProperties::henryConstant ( Real  temperature ) const

virtualinherited

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 SinglePhaseFluidProperties::henryConstant_dT().

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

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

	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

virtualinherited

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

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().

{
  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

protectedvirtualinherited

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

protectedvirtualinherited

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

virtualinherited

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 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(), 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

virtualinherited

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);
}

k_from_p_T() [1/2]

Real IdealGasFluidProperties::k_from_p_T ( Real  pressure, Real  temperature  ) const

overridevirtual

Definition at line 470 of file IdealGasFluidProperties.C.

Referenced by k_from_p_T().

{
  return _k;
}

k_from_p_T() [2/2]

void IdealGasFluidProperties::k_from_p_T ( Real  pressure, Real  temperature, Real &  k, Real &  dk_dp, Real &  dk_dT  ) const

overridevirtual

Definition at line 476 of file IdealGasFluidProperties.C.

{
  k = this->k_from_p_T(pressure, temperature);
  dk_dp = 0.0;
  dk_dT = 0.0;
}

k_from_v_e()

Real IdealGasFluidProperties::k_from_v_e ( Real  v, Real  e  ) const

overridevirtual

Definition at line 131 of file IdealGasFluidProperties.C.

{ return _k; }

molarMass()

Real IdealGasFluidProperties::molarMass ( ) const

overridevirtual

Molar mass [kg/mol].

Returns

molar mass

Reimplemented from SinglePhaseFluidProperties.

Definition at line 426 of file IdealGasFluidProperties.C.

{
  return _R / R_universal;
}

mu()

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

virtualinherited

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 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(), 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().

{
  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

virtualinherited

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

virtualinherited

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_p_T() [1/2]

Real IdealGasFluidProperties::mu_from_p_T ( Real  p, Real  T  ) const

overridevirtual

Definition at line 456 of file IdealGasFluidProperties.C.

Referenced by mu_from_p_T().

{
  return _mu;
}

mu_from_p_T() [2/2]

void IdealGasFluidProperties::mu_from_p_T ( Real  p, Real  T, Real &  mu, Real &  dmu_dp, Real &  dmu_dT  ) const

overridevirtual

Definition at line 462 of file IdealGasFluidProperties.C.

{
  mu = this->mu_from_p_T(pressure, temperature);
  dmu_dp = 0.0;
  dmu_dT = 0.0;
}

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

	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 SinglePhaseFluidProperties::mu_drhoT_from_rho_T().

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

mu_from_v_e()

Real IdealGasFluidProperties::mu_from_v_e ( Real  v, Real  e  ) const

overridevirtual

Definition at line 129 of file IdealGasFluidProperties.C.

{ return _mu; }

p_from_h_s() [1/2]

Real IdealGasFluidProperties::p_from_h_s ( Real  h, Real  s  ) const

overridevirtual

Definition at line 392 of file IdealGasFluidProperties.C.

Referenced by p_from_h_s().

{
  return std::pow(h / (_gamma * _cv), _gamma / (_gamma - 1.0)) *
         std::exp(-s / ((_gamma - 1.0) * _cv));
}

p_from_h_s() [2/2]

void IdealGasFluidProperties::p_from_h_s ( Real  h, Real  s, Real &  p, Real &  dp_dh, Real &  dp_ds  ) const

overridevirtual

Definition at line 399 of file IdealGasFluidProperties.C.

{
  p = p_from_h_s(h, s);
  dp_dh = _gamma / (_gamma - 1.0) / (_gamma * _cv) *
          std::pow(h / (_gamma * _cv), 1.0 / (_gamma - 1.0)) *
          std::exp(-s / ((_gamma - 1.0) * _cv));
  dp_ds = std::pow(h / (_gamma * _cv), _gamma / (_gamma - 1)) *
          std::exp(-s / ((_gamma - 1) * _cv)) / ((1 - _gamma) * _cv);
}

p_from_T_v() [1/2]

Real IdealGasFluidProperties::p_from_T_v ( Real  T, Real  v  ) const

overridevirtual

Definition at line 313 of file IdealGasFluidProperties.C.

Referenced by s_from_T_v().

{
  return (_gamma - 1.0) * _cv * T / v;
}

p_from_T_v() [2/2]

void IdealGasFluidProperties::p_from_T_v ( Real  T, Real  v, Real &  p, Real &  dp_dT, Real &  dp_dv  ) const

overridevirtual

Definition at line 319 of file IdealGasFluidProperties.C.

{
  p = (_gamma - 1.0) * _cv * T / v;
  dp_dT = (_gamma - 1.0) * _cv / v;
  dp_dv = -(_gamma - 1.0) * _cv * T / (v * v);
}

p_from_v_e() [1/2]

Real IdealGasFluidProperties::p_from_v_e ( Real  v, Real  e  ) const

overridevirtual

Definition at line 42 of file IdealGasFluidProperties.C.

Referenced by NSPressureAux::computeValue(), g_from_v_e(), p_from_v_e(), and s_from_v_e().

{
  if (v == 0.0)
    throw MooseException(
        name() + ": Invalid value of specific volume detected (v = " + Moose::stringify(v) + ").");

  return (_gamma - 1.0) * e / v;
}

p_from_v_e() [2/2]

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

overridevirtual

Definition at line 52 of file IdealGasFluidProperties.C.

{
  p = p_from_v_e(v, e);
  dp_dv = -(_gamma - 1.0) * e / v / v;
  dp_de = (_gamma - 1.0) / v;
}

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]	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

virtualinherited

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

virtualinherited

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

virtualinherited

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 SinglePhaseFluidProperties::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_from_p_s() [1/2]

Real IdealGasFluidProperties::rho_from_p_s ( Real  p, Real  s  ) const

overridevirtual

Definition at line 217 of file IdealGasFluidProperties.C.

{
  const Real aux = (s + _cv * std::log(std::pow(p, _gamma - 1.0))) / _cv;
  const Real T = std::pow(std::exp(aux), 1.0 / _gamma);
  return rho_from_p_T(p, T);
}

rho_from_p_s() [2/2]

void IdealGasFluidProperties::rho_from_p_s ( Real  p, Real  s, Real &  rho, Real &  drho_dp, Real &  drho_ds  ) const

overridevirtual

Definition at line 225 of file IdealGasFluidProperties.C.

{
  // T(p,s)
  const Real aux = (s + _cv * std::log(std::pow(p, _gamma - 1.0))) / _cv;
  const Real T = std::pow(std::exp(aux), 1 / _gamma);

  // dT/dp
  const Real dT_dp = 1.0 / _gamma * std::pow(std::exp(aux), 1.0 / _gamma - 1.0) * std::exp(aux) /
                     std::pow(p, _gamma - 1.0) * (_gamma - 1.0) * std::pow(p, _gamma - 2.0);

  // dT/ds
  const Real dT_ds =
      1.0 / _gamma * std::pow(std::exp(aux), 1.0 / _gamma - 1.0) * std::exp(aux) / _cv;

  // Drho/Dp = d/dp[rho(p, T(p,s))] = drho/dp + drho/dT * dT/dp
  Real drho_dp_partial, drho_dT;
  rho_from_p_T(p, T, rho, drho_dp_partial, drho_dT);
  drho_dp = drho_dp_partial + drho_dT * dT_dp;

  // Drho/Ds = d/ds[rho(p, T(p,s))] = drho/dT * dT/ds
  drho_ds = drho_dT * dT_ds;
}

rho_from_p_T() [1/2]

Real IdealGasFluidProperties::rho_from_p_T ( Real  p, Real  T  ) const

overridevirtual

Definition at line 264 of file IdealGasFluidProperties.C.

Referenced by h_from_p_T(), rho_from_p_s(), rho_from_p_T(), NSWeakStagnationBaseBC::staticValues(), and NSInitialCondition::value().

{
  if ((_gamma - 1.0) * p == 0.0)
    throw MooseException(name() +
                         ": Invalid gamma or pressure detected in rho_from_p_T(pressure = " +
                         Moose::stringify(p) + ", gamma = " + Moose::stringify(_gamma) + ")");

  return p / (_gamma - 1.0) / _cv / T;
}

rho_from_p_T() [2/2]

void IdealGasFluidProperties::rho_from_p_T ( Real  p, Real  T, Real &  rho, Real &  drho_dp, Real &  drho_dT  ) const

overridevirtual

Definition at line 275 of file IdealGasFluidProperties.C.

{
  rho = rho_from_p_T(p, T);
  drho_dp = 1.0 / (_gamma - 1.0) / _cv / T;
  drho_dT = -p / (_gamma - 1.0) / _cv / (T * T);
}

rho_mu()

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

virtualinherited

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

virtualinherited

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

virtualinherited

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(), SinglePhaseFluidProperties::rho_mu(), and SinglePhaseFluidProperties::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

virtualinherited

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

virtualinherited

Definition at line 421 of file SinglePhaseFluidProperties.C.

Referenced by p_from_h_s(), StiffenedGasFluidProperties::p_from_h_s(), StiffenedGasFluidProperties::rho_from_p_s(), rho_from_p_s(), StiffenedGasFluidProperties::s_from_h_p(), s_from_h_p(), 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(), s_from_T_v(), s_from_v_e(), StiffenedGasFluidProperties::s_from_v_e(), and SinglePhaseFluidProperties::T_from_p_h().

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

  return s_from_p_T(p, T);
}

s_from_h_p() [1/2]

Real IdealGasFluidProperties::s_from_h_p ( Real  h, Real  p  ) const

overridevirtual

Definition at line 195 of file IdealGasFluidProperties.C.

Referenced by s_from_h_p().

{
  const Real aux = p * std::pow(h / (_gamma * _cv), -_gamma / (_gamma - 1));
  if (aux <= 0.0)
    throw MooseException(name() + ": Non-positive argument in the ln() function.");
  return -(_gamma - 1) * _cv * std::log(aux);
}

s_from_h_p() [2/2]

void IdealGasFluidProperties::s_from_h_p ( Real  h, Real  p, Real &  s, Real &  ds_dh, Real &  ds_dp  ) const

overridevirtual

Definition at line 204 of file IdealGasFluidProperties.C.

{
  s = s_from_h_p(h, p);

  const Real aux = p * std::pow(h / (_gamma * _cv), -_gamma / (_gamma - 1));
  const Real daux_dh = p * std::pow(h / (_gamma * _cv), -_gamma / (_gamma - 1) - 1) *
                       (-_gamma / (_gamma - 1)) / (_gamma * _cv);
  const Real daux_dp = std::pow(h / (_gamma * _cv), -_gamma / (_gamma - 1));
  ds_dh = -(_gamma - 1) * _cv / aux * daux_dh;
  ds_dp = -(_gamma - 1) * _cv / aux * daux_dp;
}

s_from_p_T() [1/2]

Real IdealGasFluidProperties::s_from_p_T ( Real  p, Real  T  ) const

overridevirtual

Definition at line 170 of file IdealGasFluidProperties.C.

Referenced by s_from_T_v().

{
  const Real n = std::pow(T, _gamma) / std::pow(p, _gamma - 1.0);
  if (n <= 0.0)
    throw MooseException(name() + ": Negative argument in the ln() function.");
  return _cv * std::log(n);
}

s_from_p_T() [2/2]

void IdealGasFluidProperties::s_from_p_T ( Real  p, Real  T, Real &  s, Real &  ds_dp, Real &  ds_dT  ) const

overridevirtual

Definition at line 179 of file IdealGasFluidProperties.C.

{
  const Real n = std::pow(T, _gamma) / std::pow(p, _gamma - 1.0);
  if (n <= 0.0)
    throw MooseException(name() + ": Negative argument in the ln() function.");

  s = _cv * std::log(n);

  const Real dn_dT = _gamma * std::pow(T, _gamma - 1.0) / std::pow(p, _gamma - 1.0);
  const Real dn_dp = std::pow(T, _gamma) * (1.0 - _gamma) * std::pow(p, -_gamma);

  ds_dp = _cv / n * dn_dp;
  ds_dT = _cv / n * dn_dT;
}

s_from_T_v() [1/2]

Real IdealGasFluidProperties::s_from_T_v ( Real  T, Real  v  ) const

overridevirtual

Definition at line 341 of file IdealGasFluidProperties.C.

{
  Real p = p_from_T_v(T, v);
  return s_from_p_T(p, T);
}

s_from_T_v() [2/2]

void IdealGasFluidProperties::s_from_T_v ( Real  T, Real  v, Real &  s, Real &  ds_dT, Real &  ds_dv  ) const

overridevirtual

Definition at line 348 of file IdealGasFluidProperties.C.

{
  Real p, dp_dT_v, dp_dv_T;
  Real ds_dp_T, ds_dT_p;
  p_from_T_v(T, v, p, dp_dT_v, dp_dv_T);
  s_from_p_T(p, T, s, ds_dp_T, ds_dT_p);
  ds_dT = ds_dT_p + ds_dp_T * dp_dT_v;
  ds_dv = ds_dp_T * dp_dv_T;
}

s_from_v_e() [1/2]

Real IdealGasFluidProperties::s_from_v_e ( Real  v, Real  e  ) const

overridevirtual

Definition at line 134 of file IdealGasFluidProperties.C.

{
  const Real T = T_from_v_e(v, e);
  const Real p = p_from_v_e(v, e);
  const Real n = std::pow(T, _gamma) / std::pow(p, _gamma - 1.0);
  if (n <= 0.0)
    throw MooseException(name() + ": Negative argument in the ln() function.");
  return _cv * std::log(n);
}

s_from_v_e() [2/2]

void IdealGasFluidProperties::s_from_v_e ( Real  v, Real  e, Real &  s, Real &  ds_dv, Real &  ds_de  ) const

overridevirtual

Definition at line 145 of file IdealGasFluidProperties.C.

{
  Real T, dT_dv, dT_de;
  T_from_v_e(v, e, T, dT_dv, dT_de);

  Real p, dp_dv, dp_de;
  p_from_v_e(v, e, p, dp_dv, dp_de);

  const Real n = std::pow(T, _gamma) / std::pow(p, _gamma - 1.0);
  if (n <= 0.0)
    throw MooseException(name() + ": Negative argument in the ln() function.");

  s = _cv * std::log(n);

  const Real dn_dT = _gamma * std::pow(T, _gamma - 1.0) / std::pow(p, _gamma - 1.0);
  const Real dn_dp = std::pow(T, _gamma) * (1.0 - _gamma) * std::pow(p, -_gamma);

  const Real dn_dv = dn_dT * dT_dv + dn_dp * dp_dv;
  const Real dn_de = dn_dT * dT_de + dn_dp * dp_de;

  ds_dv = _cv / n * dn_dv;
  ds_de = _cv / n * dn_de;
}

subdomainSetup()

virtual void FluidProperties::subdomainSetup ( )

inlinefinalvirtualinherited

Definition at line 32 of file FluidProperties.h.

{}

T_from_p_h()

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

overridevirtual

Temperature from pressure and specific enthalpy.

Parameters

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

Returns

Temperature (K)

Reimplemented from SinglePhaseFluidProperties.

Definition at line 432 of file IdealGasFluidProperties.C.

{
  return h / _gamma / _cv;
}

T_from_v_e() [1/2]

Real IdealGasFluidProperties::T_from_v_e ( Real  v, Real  e  ) const

overridevirtual

Definition at line 60 of file IdealGasFluidProperties.C.

Referenced by c_from_v_e(), NSTemperatureAux::computeValue(), g_from_v_e(), s_from_v_e(), and T_from_v_e().

{
  return e / _cv;
}

T_from_v_e() [2/2]

void IdealGasFluidProperties::T_from_v_e ( Real  v, Real  e, Real &  T, Real &  dT_dv, Real &  dT_de  ) const

overridevirtual

Definition at line 66 of file IdealGasFluidProperties.C.

{
  T = T_from_v_e(v, e);
  dT_dv = 0.0;
  dT_de = 1.0 / _cv;
}

threadJoin()

virtual void FluidProperties::threadJoin ( const UserObject &  )

inlinefinalvirtualinherited

Definition at line 31 of file FluidProperties.h.

{}

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.

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

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.

{
  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

virtualinherited

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

virtualinherited

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

virtualinherited

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

virtualinherited

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 SinglePhaseFluidProperties::vaporPressure_dT().

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

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

	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

virtualinherited

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

_cp

Real IdealGasFluidProperties::_cp

protected

Definition at line 95 of file IdealGasFluidProperties.h.

Referenced by cp(), cp_from_p_T(), cp_from_v_e(), and IdealGasFluidProperties().

_cv

Real IdealGasFluidProperties::_cv

protected

Definition at line 94 of file IdealGasFluidProperties.h.

Referenced by cv(), cv_from_p_T(), cv_from_T_v(), cv_from_v_e(), e_from_p_T(), e_from_T_v(), g_from_v_e(), h_from_p_T(), h_from_T_v(), IdealGasFluidProperties(), p_from_h_s(), p_from_T_v(), rho_from_p_s(), rho_from_p_T(), s_from_h_p(), s_from_p_T(), s_from_v_e(), T_from_p_h(), and T_from_v_e().

_gamma

Real IdealGasFluidProperties::_gamma

protected

Definition at line 92 of file IdealGasFluidProperties.h.

Referenced by c_from_v_e(), e_from_p_rho(), e_from_v_h(), g_from_v_e(), gamma(), h_from_T_v(), IdealGasFluidProperties(), p_from_h_s(), p_from_T_v(), p_from_v_e(), rho_from_p_s(), rho_from_p_T(), s_from_h_p(), s_from_p_T(), s_from_v_e(), and T_from_p_h().

_k

Real IdealGasFluidProperties::_k

protected

Definition at line 98 of file IdealGasFluidProperties.h.

Referenced by k_from_p_T(), and k_from_v_e().

_mu

Real IdealGasFluidProperties::_mu

protected

Definition at line 97 of file IdealGasFluidProperties.h.

Referenced by mu_from_p_T(), and mu_from_v_e().

_R

Real IdealGasFluidProperties::_R

protected

Definition at line 93 of file IdealGasFluidProperties.h.

Referenced by c_from_v_e(), IdealGasFluidProperties(), and molarMass().

_T_c2k

const Real SinglePhaseFluidProperties::_T_c2k

protectedinherited

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

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(), e_from_p_rho(), e_from_p_T(), StiffenedGasFluidProperties::e_from_p_T(), SinglePhaseFluidProperties::e_from_p_T(), g_from_v_e(), StiffenedGasFluidProperties::g_from_v_e(), SinglePhaseFluidProperties::gamma_from_p_T(), TabulatedFluidProperties::generateTabulatedData(), SinglePhaseFluidProperties::h(), SinglePhaseFluidProperties::h_dpT(), h_from_p_T(), StiffenedGasFluidProperties::h_from_p_T(), SinglePhaseFluidProperties::henryConstantIAPWS(), SinglePhaseFluidProperties::k(), SinglePhaseFluidProperties::k_dpT(), SinglePhaseFluidProperties::mu(), SinglePhaseFluidProperties::mu_dpT(), p_from_h_s(), StiffenedGasFluidProperties::p_from_h_s(), StiffenedGasFluidProperties::p_from_T_v(), p_from_T_v(), 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(), rho_from_p_s(), StiffenedGasFluidProperties::rho_from_p_T(), rho_from_p_T(), SinglePhaseFluidProperties::rho_mu(), SinglePhaseFluidProperties::rho_mu_dpT(), SinglePhaseFluidProperties::rho_mu_from_p_T(), SinglePhaseFluidProperties::s(), StiffenedGasFluidProperties::s_from_h_p(), s_from_h_p(), 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(), s_from_T_v(), StiffenedGasFluidProperties::s_from_v_e(), 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.

R_universal

constexpr Real IdealGasFluidProperties::R_universal = 8.3144598

staticprotected

Universal gas constant [J/K.mol].

Definition at line 101 of file IdealGasFluidProperties.h.

Referenced by molarMass().

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(), e_from_p_rho(), NaClFluidProperties::e_from_p_T(), SinglePhaseFluidProperties::e_from_p_T(), 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(), 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(), 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(), c_from_v_e(), SinglePhaseFluidProperties::e(), SinglePhaseFluidProperties::e_dpT(), e_from_p_T(), StiffenedGasFluidProperties::e_from_p_T(), SinglePhaseFluidProperties::e_from_p_T(), StiffenedGasFluidProperties::e_from_T_v(), e_from_T_v(), g_from_v_e(), StiffenedGasFluidProperties::g_from_v_e(), SinglePhaseFluidProperties::gamma_from_p_T(), SinglePhaseFluidProperties::h(), SinglePhaseFluidProperties::h_dpT(), h_from_p_T(), StiffenedGasFluidProperties::h_from_p_T(), StiffenedGasFluidProperties::h_from_T_v(), 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(), p_from_T_v(), SinglePhaseFluidProperties::rho_dpT(), SinglePhaseFluidProperties::rho_e_dpT(), SinglePhaseFluidProperties::rho_e_from_p_T(), rho_from_p_s(), StiffenedGasFluidProperties::rho_from_p_s(), StiffenedGasFluidProperties::rho_from_p_T(), rho_from_p_T(), SinglePhaseFluidProperties::rho_mu(), SinglePhaseFluidProperties::rho_mu_dpT(), SinglePhaseFluidProperties::rho_mu_from_p_T(), SinglePhaseFluidProperties::s(), 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(), s_from_T_v(), StiffenedGasFluidProperties::s_from_v_e(), s_from_v_e(), 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

Definition at line 122 of file SinglePhaseFluidProperties.h.

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

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.

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

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