FlibeFluidProperties Class Reference

Fluid properties for 2LiF-BeF2 (flibe) [richard]. More...

#include <FlibeFluidProperties.h>

Inheritance diagram for FlibeFluidProperties:

Public Member Functions
	FlibeFluidProperties (const InputParameters &parameters)
virtual std::string	fluidName () const override
	Fluid name. More...
virtual Real	p_from_v_e (Real v, Real e) const override
	Pressure from specific volume and specific internal energy. More...
virtual void	p_from_v_e (Real v, Real e, Real &p, Real &dp_dv, Real &dp_de) const override
	Pressure and its derivatives from specific volume and specific internal energy. More...
virtual void	p_from_v_e (const DualReal &v, const DualReal &e, DualReal &p, DualReal &dp_dv, DualReal &dp_de) const override
virtual Real	T_from_v_e (Real v, Real e) const override
	Temperature from specific volume and specific internal energy. More...
virtual void	T_from_v_e (Real v, Real e, Real &T, Real &dT_dv, Real &dT_de) const override
	Temperature and its derivatives from specific volume and specific internal energy. More...
virtual void	T_from_v_e (const DualReal &v, const DualReal &e, DualReal &T, DualReal &dT_dv, DualReal &dT_de) const override
virtual Real	cp_from_v_e (Real v, Real e) const override
	Isobaric specific heat from specific volume and specific internal energy. More...
virtual void	cp_from_v_e (Real v, Real e, Real &cp, Real &dcp_dv, Real &dcp_de) const override
	Isobaric specific heat and its derivatives from specific volume and specific internal energy. More...
virtual Real	cv_from_v_e (Real v, Real e) const override
	Isochoric specific heat from specific volume and specific internal energy. More...
virtual void	cv_from_v_e (Real v, Real e, Real &cv, Real &dcv_dv, Real &dcv_de) const override
	Isochoric specific heat and its derivatives from specific volume and specific internal energy. More...
virtual void	cv_from_v_e (const DualReal &v, const DualReal &e, DualReal &cv, DualReal &dcv_dv, DualReal &dcv_de) const override
virtual Real	mu_from_v_e (Real v, Real e) const override
	Dynamic viscosity from specific volume and specific internal energy. More...
virtual Real	k_from_v_e (Real v, Real e) const override
	Thermal conductivity from specific volume and specific internal energy. More...
virtual Real	rho_from_p_T (Real p, Real T) const override
	Density from pressure and temperature. More...
virtual void	rho_from_p_T (Real p, Real T, Real &rho, Real &drho_dp, Real &drho_dT) const override
	Density and its derivatives from pressure and temperature. More...
virtual void	rho_from_p_T (const DualReal &p, const DualReal &T, DualReal &rho, DualReal &drho_dp, DualReal &drho_dT) const override
virtual Real	v_from_p_T (Real p, Real T) const override
	Specific volume from pressure and temperature. More...
virtual DualReal	v_from_p_T (const DualReal &p, const DualReal &T) const override
virtual void	v_from_p_T (Real p, Real T, Real &v, Real &dv_dp, Real &dv_dT) const override
	Specific volume and its derivatives from pressure and temperature. More...
virtual Real	h_from_p_T (Real p, Real T) const override
	Specific enthalpy from pressure and temperature. More...
virtual void	h_from_p_T (Real p, Real T, Real &h, Real &dh_dp, Real &dh_dT) const override
	Specific enthalpy and its derivatives from pressure and temperature. More...
virtual Real	e_from_p_T (Real p, Real T) const override
	Specific 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
	Specific internal energy and its derivatives from pressure and temperature. More...
virtual Real	cp_from_p_T (Real p, Real T) const override
	Isobaric specific heat capacity from pressure and temperature. More...
virtual void	cp_from_p_T (Real p, Real T, Real &cp, Real &dcp_dp, Real &dcp_dT) const override
	Isobaric specific heat capacity and its derivatives from pressure and temperature. More...
virtual Real	cv_from_p_T (Real p, Real T) const override
	Isochoric specific heat capacity from pressure and temperature. More...
virtual void	cv_from_p_T (Real p, Real T, Real &cv, Real &dcv_dp, Real &dcv_dT) const override
virtual Real	molarMass () const override
	Molar mass. More...
virtual Real	k_from_p_T (Real p, Real T) const override
	Thermal conductivity from pressure and temperature. More...
virtual void	k_from_p_T (Real p, Real T, Real &k, Real &dk_dp, Real &dk_dT) const override
	Thermal conductivity and its derivatives wrt pressure and temperature. More...
virtual Real	mu_from_p_T (Real p, Real T) const override
	Dynamic viscosity from pressure and temperature. More...
virtual void	mu_from_p_T (Real p, Real T, Real &mu, Real &dmu_drho, Real &dmu_dT) const override
	Dynamic viscosity and its derivatives wrt pressure and temperature. 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 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	vaporPressure (Real T) const
	Vapor pressure. More...
virtual void	vaporPressure (Real T, Real &psat, Real &dpsat_dT) const
DualReal	vaporPressure (const DualReal &T) const
virtual Real	vaporTemperature (Real p) const
	Vapor temperature. More...
virtual void	vaporTemperature (Real p, Real &Tsat, Real &dTsat_dp) const
DualReal	vaporTemperature (const DualReal &p) const
virtual std::vector< Real >	henryCoefficients () const
	Henry's law coefficients for dissolution in water. More...
virtual void	rho_mu_from_p_T (Real p, Real T, Real &rho, Real &mu) const
	Combined methods. More...
virtual void	rho_mu_from_p_T (Real p, Real T, Real &rho, Real &drho_dp, Real &drho_dT, Real &mu, Real &dmu_dp, Real &dmu_dT) const
virtual void	rho_mu_from_p_T (const DualReal &p, const DualReal &T, DualReal &rho, DualReal &mu) const
virtual void	rho_e_from_p_T (Real p, Real T, Real &rho, Real &drho_dp, Real &drho_dT, Real &e, Real &de_dp, Real &de_dT) const
virtual void	execute () final
virtual void	initialize () final
virtual void	finalize () final
virtual void	threadJoin (const UserObject &) final
virtual void	subdomainSetup () final

Static Public Attributes
static const Real	_R = 8.3144598
	Universal gas constant (J/mol/K) More...

Protected Attributes
const Real &	_drho_dp
	Derivative of density with respect to pressure at fixed temperature. More...
const Real	_drho_dT
	Derivative of density with respect to temperature at fixed pressure. More...
const Real	_p_atm
	Atmospheric pressure, Pa. More...
const Real	_cp
	specific heat at constant pressure More...
const Real	_c0
	additive constant to rho(P, T) correlation More...
const Real	_dp_dT_at_constant_v
	derivative of pressure with respect to temperature at constant specific volume More...
const Real	_T_c2k
	Conversion of temperature from Celsius to Kelvin. More...
const bool	_allow_imperfect_jacobians
	Flag to set unimplemented Jacobian entries to zero. More...

Private Member Functions
template<typename... Args>
void	fluidPropError (Args... args) const
e e e e p h T T T T T v v v s h	propfuncWithDefault (beta, p, T) propfuncWithDefault(v
e e e e p h T T T T T v v v s h T	propfuncWithDefault (e, p, T) propfuncWithDefault(gamma
	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(T
e e e e p	propfunc (rho, p, s) propfunc(e
e e e e p h	propfunc (s, p, T) propfunc(pp_sat
e e e e p h T	propfunc (mu, rho, T) propfunc(k
e e e e p h T T	propfunc (c, p, T) propfunc(cp
e e e e p h T T T	propfunc (cv, p, T) propfunc(mu
e e e e p h T T T T	propfunc (k, p, T) propfunc(rho
e e e e p h T T T T T	propfunc (e, p, rho) propfunc(e
e e e e p h T T T T T v	propfunc (p, T, v) propfunc(h
e e e e p h T T T T T v v	propfunc (s, T, v) propfunc(cv
e e e e p h T T T T T v v v	propfunc (h, p, T) propfunc(p
e e e e p h T T T T T v v v s	propfunc (g, v, e) propfuncWithDefault(T
	v
e	v
e e	v
e e e	v
e e e e p	v
e e e e p h T T T T T v v v s h T	v
e e e e	h
e e e e p h T T T T T v v v	h
e e e e p h	p
e e e e p h T T	p
e e e e p h T T T	p
e e e e p h T T T T	p
e e e e p h T T T T T v v v s	p
e e e e p h T T T T T v v v s h	p
e e e e p h T	rho
e e e e p h T T T T T	T
e e e e p h T T T T T v	T
e e e e p h T T T T T v v	T
e e e e p h T T T T T v v v s h T e	propfuncWithDefault (gamma, p, T)

Detailed Description

Fluid properties for 2LiF-BeF2 (flibe) [richard].

Definition at line 22 of file FlibeFluidProperties.h.

Constructor & Destructor Documentation

FlibeFluidProperties()

FlibeFluidProperties::FlibeFluidProperties

(

const InputParameters &

parameters

)

Definition at line 28 of file FlibeFluidProperties.C.

  : SinglePhaseFluidProperties(parameters),
    _drho_dp(getParam<Real>("drho_dp")),
    _drho_dT(-0.4884),
    _p_atm(101325.0),
    _cp(2416.0),
    _c0(2413.0),
    _dp_dT_at_constant_v(-_drho_dT / _drho_dp)
{
}

Member Function Documentation

cp_from_p_T() [1/2]

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

overridevirtual

Isobaric specific heat capacity from pressure and temperature.

Parameters

p	pressure (Pa)
T	temperature (K)

Returns

isobaric specific heat (J/kg/.K)

Definition at line 291 of file FlibeFluidProperties.C.

{
  return _cp;
}

Referenced by cp_from_p_T().

cp_from_p_T() [2/2]

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

overridevirtual

Isobaric specific heat capacity and its derivatives from pressure and temperature.

Parameters

[in]	p	pressure (Pa)
[in]	T	temperature (K)
[out]	cp	isobaric specific heat (J/kg/K)
[out]	dcp_dp	derivative of isobaric specific heat w.r.t. pressure (J/kg/K/Pa)

Definition at line 297 of file FlibeFluidProperties.C.

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

cp_from_v_e() [1/2]

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

overridevirtual

Isobaric specific heat from specific volume and specific internal energy.

Parameters

[in]	v	specific volume (m$^3$/kg)
[in]	e	specific internal energy (J/kg)

Returns

isobaric specific heat (J/kg.K)

Definition at line 146 of file FlibeFluidProperties.C.

{ return _cp; }

Referenced by cp_from_v_e(), cv_from_v_e(), e_from_p_T(), h_from_p_T(), p_from_v_e(), and T_from_v_e().

cp_from_v_e() [2/2]

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

overridevirtual

Isobaric specific heat and its derivatives from specific volume and specific internal energy.

Parameters

[in]	v	specific volume (m$^3$/kg)
[in]	e	specific internal energy (J/kg)
[out]	cp	isobaric specific heat (J/kg.K)
[out]	dcp_dv	derivative of isobaric specific heat w.r.t. specific volume
[out]	dcp_de	derivative of isobaric specific heat w.r.t. specific internal energy

Definition at line 149 of file FlibeFluidProperties.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 IdealGasFluidProperties, CO2FluidProperties, HydrogenFluidProperties, NitrogenFluidProperties, StiffenedGasFluidProperties, MethaneFluidProperties, NaClFluidProperties, and Water97FluidProperties.

Definition at line 120 of file SinglePhaseFluidProperties.C.

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

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(), IdealRealGasMixtureFluidProperties::T_from_p_v(), and IdealRealGasMixtureFluidProperties::v_from_p_T().

criticalInternalEnergy()

Real SinglePhaseFluidProperties::criticalInternalEnergy ( ) const

virtualinherited

Critical specific internal energy.

Returns

specific internal energy (J/kg)

Reimplemented in IdealGasFluidProperties, and StiffenedGasFluidProperties.

Definition at line 126 of file SinglePhaseFluidProperties.C.

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

Referenced by IdealRealGasMixtureFluidProperties::p_T_from_v_e(), and IdealRealGasMixtureFluidProperties::T_from_p_v().

criticalPressure()

Real SinglePhaseFluidProperties::criticalPressure ( ) const

virtualinherited

Critical pressure.

Returns

critical pressure (Pa)

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

Definition at line 108 of file SinglePhaseFluidProperties.C.

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

criticalTemperature()

Real SinglePhaseFluidProperties::criticalTemperature ( ) const

virtualinherited

Critical temperature.

Returns

critical temperature (K)

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

Definition at line 114 of file SinglePhaseFluidProperties.C.

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

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().

cv_from_p_T() [1/2]

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

overridevirtual

Isochoric specific heat capacity from pressure and temperature.

Parameters

p	pressure (Pa)
T	temperature (K)

Returns

isochoric specific heat (J/kg.K)

Definition at line 306 of file FlibeFluidProperties.C.

{
  Real v = v_from_p_T(pressure, temperature);
  Real e = e_from_p_T(pressure, temperature);
  return cv_from_v_e(v, e);
}

Referenced by cv_from_p_T().

cv_from_p_T() [2/2]

void FlibeFluidProperties::cv_from_p_T ( Real  p, Real  T, Real &  cv, Real &  dcv_dp, Real &  dcv_dT  ) const

overridevirtual

Definition at line 314 of file FlibeFluidProperties.C.

{
  cv = cv_from_p_T(pressure, temperature);
  dcv_dp = 0.0;
  dcv_dT = 0.0;
}

cv_from_v_e() [1/3]

void FlibeFluidProperties::cv_from_v_e ( const DualReal &  v, const DualReal &  e, DualReal &  cv, DualReal &  dcv_dv, DualReal &  dcv_de  ) const

overridevirtual

Definition at line 173 of file FlibeFluidProperties.C.

{
  cv = SinglePhaseFluidProperties::cv_from_v_e(v, e);
  dcv_dv = -_dp_dT_at_constant_v;
  dcv_de = 0.0;
}

cv_from_v_e() [2/3]

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

overridevirtual

Isochoric specific heat from specific volume and specific internal energy.

Parameters

[in]	v	specific volume (m$^3$/kg)
[in]	e	specific internal energy (J/kg)

Returns

isochoric specific heat (J/kg.K)

Definition at line 157 of file FlibeFluidProperties.C.

{
  // definition of Cv by replacing e by h + p * v
  Real cp = cp_from_v_e(v, e);
  return cp - _dp_dT_at_constant_v * v;
}

Referenced by cv_from_p_T(), cv_from_v_e(), and T_from_v_e().

cv_from_v_e() [3/3]

void FlibeFluidProperties::cv_from_v_e ( Real  v, Real  e, Real &  cv, Real &  dcv_dv, Real &  dcv_de  ) const

overridevirtual

Isochoric specific heat and its derivatives from specific volume and specific internal energy.

Parameters

[in]	v	specific volume (m$^3$/kg)
[in]	e	specific internal energy (J/kg)
[out]	cv	isochoric specific heat (J/kg.K)
[out]	dcv_dv	derivative of isochoric specific heat w.r.t. specific volume
[out]	dcv_de	derivative of isochoric specific heat w.r.t. specific internal energy

Definition at line 165 of file FlibeFluidProperties.C.

{
  cv = cv_from_v_e(v, e);
  dcv_dv = -_dp_dT_at_constant_v;
  dcv_de = 0.0;
}

e_from_p_T() [1/2]

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

overridevirtual

Specific internal energy from pressure and temperature.

Parameters

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

Returns

specific internal energy (J/kg)

Definition at line 266 of file FlibeFluidProperties.C.

{
  // definition of h = e + p * v
  Real v = v_from_p_T(pressure, temperature);
  Real cp = cp_from_v_e(v, 0.0 /* dummy */);
  return cp * temperature - pressure * v;
}

Referenced by cv_from_p_T(), and e_from_p_T().

e_from_p_T() [2/2]

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

overridevirtual

Specific internal energy and its derivatives from pressure and temperature.

Parameters

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

Definition at line 275 of file FlibeFluidProperties.C.

{
  e = e_from_p_T(pressure, temperature);
 
  Real v, dv_dp, dv_dT;
  v_from_p_T(pressure, temperature, v, dv_dp, dv_dT);
 
  // definition of e = h - p * v
  de_dp = -pressure * dv_dp - v;
 
  // definition of e = h - p * v
  Real cp = cp_from_v_e(v, e);
  de_dT = cp - pressure * dv_dT;
}

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 IdealGasFluidProperties, and StiffenedGasFluidProperties.

Definition at line 286 of file SinglePhaseFluidProperties.C.

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

Referenced by IdealRealGasMixtureFluidProperties::p_T_from_v_e(), and IdealRealGasMixtureFluidProperties::T_from_p_v().

execute()

virtual void FluidProperties::execute ( )

inlinefinalvirtualinherited

Definition at line 34 of file FluidProperties.h.

{}

finalize()

virtual void FluidProperties::finalize ( )

inlinefinalvirtualinherited

Definition at line 36 of file FluidProperties.h.

{}

fluidName()

std::string FlibeFluidProperties::fluidName ( ) const

overridevirtual

Fluid name.

Returns

"flibe"

Definition at line 40 of file FlibeFluidProperties.C.

{
  return "flibe";
}

fluidPropError()

template<typename... Args>

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

inlineprivateinherited

Definition at line 326 of file SinglePhaseFluidProperties.h.

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

Referenced by SinglePhaseFluidProperties::vaporPressure(), and SinglePhaseFluidProperties::vaporTemperature().

h_from_p_T() [1/2]

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

overridevirtual

Specific enthalpy from pressure and temperature.

Parameters

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

Returns

specific enthalpy (J/kg)

Definition at line 247 of file FlibeFluidProperties.C.

{
  // definition of h for constant Cp
  Real cp = cp_from_v_e(0.0 /* dummy */, 0.0 /* dummy */);
  return cp * temperature;
}

Referenced by h_from_p_T().

h_from_p_T() [2/2]

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

overridevirtual

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 255 of file FlibeFluidProperties.C.

{
  h = h_from_p_T(pressure, temperature);
  Real cp = cp_from_v_e(0.0 /* dummy */, 0.0 /* dummy */);
 
  dh_dp = 0.0;
  dh_dT = cp;
}

henryCoefficients()

std::vector< Real > SinglePhaseFluidProperties::henryCoefficients ( ) const

virtualinherited

Henry's law coefficients for dissolution in water.

Returns

Henry's constant coefficients

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

Definition at line 183 of file SinglePhaseFluidProperties.C.

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

Referenced by TabulatedFluidProperties::henryCoefficients().

initialize()

virtual void FluidProperties::initialize ( )

inlinefinalvirtualinherited

Definition at line 35 of file FluidProperties.h.

{}

k_from_p_T() [1/2]

Real FlibeFluidProperties::k_from_p_T ( Real  p, Real  T  ) const

overridevirtual

Thermal conductivity from pressure and temperature.

Parameters

p	pressure (Pa)
T	temperature (K)

Returns

thermal conductivity (W/m.K)

Definition at line 338 of file FlibeFluidProperties.C.

{
  return 5.0e-4 * temperature + 0.63;
}

Referenced by k_from_p_T().

k_from_p_T() [2/2]

void FlibeFluidProperties::k_from_p_T ( Real  p, Real  T, Real &  k, Real &  dk_dp, Real &  dk_dT  ) const

overridevirtual

Thermal conductivity and its derivatives wrt pressure and temperature.

Parameters

	p	pressure (Pa)
	T	temperature (K)
[out]	k	thermal conductivity (W/m.K)
[out]	dk_dp	derivative of thermal conductivity wrt pressure
[out]	dk_dT	derivative of thermal conductivity wrt temperature

Definition at line 344 of file FlibeFluidProperties.C.

{
  k = this->k_from_p_T(pressure, temperature);
  dk_dp = 0.0;
  dk_dT = 5.0e-4;
}

k_from_v_e()

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

overridevirtual

Thermal conductivity from specific volume and specific internal energy.

Parameters

[in]	v	specific volume (m$^3$/kg)
[in]	e	specific internal energy (J/kg)

Returns

thermal conductivity (W/m.K)

Definition at line 192 of file FlibeFluidProperties.C.

{
  Real temperature = T_from_v_e(v, e);
  return 5.0e-4 * temperature + 0.63;
}

molarMass()

Real FlibeFluidProperties::molarMass ( ) const

overridevirtual

Molar mass.

Returns

molar mass (kg/mol)

Reimplemented from SinglePhaseFluidProperties.

Definition at line 46 of file FlibeFluidProperties.C.

{
  return 99.037703E-3;
}

mu_from_p_T() [1/2]

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

overridevirtual

Dynamic viscosity from pressure and temperature.

Parameters

p	pressure (Pa)
T	temperature (K)

Returns

dynamic viscosity (Pa.s)

Definition at line 323 of file FlibeFluidProperties.C.

{
  return 1.16e-4 * std::exp(3755.0 / temperature);
}

Referenced by mu_from_p_T().

mu_from_p_T() [2/2]

void FlibeFluidProperties::mu_from_p_T ( Real  p, Real  T, Real &  mu, Real &  dmu_drho, Real &  dmu_dT  ) const

overridevirtual

Dynamic viscosity and its derivatives wrt pressure and temperature.

Parameters

	p	pressure (Pa)
	T	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 329 of file FlibeFluidProperties.C.

{
  mu = this->mu_from_p_T(pressure, temperature);
  dmu_dp = 0.0;
  dmu_dT = -1.16e-4 * std::exp(3755.0 / temperature) * 3755.0 / (temperature * temperature);
}

mu_from_v_e()

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

overridevirtual

Dynamic viscosity from specific volume and specific internal energy.

Parameters

[in]	v	specific volume (m$^3$/kg)
[in]	e	specific internal energy (J/kg)

Returns

dynamic viscosity (Pa.s)

Definition at line 185 of file FlibeFluidProperties.C.

{
  Real temperature = T_from_v_e(v, e);
  return 1.16e-4 * std::exp(3755.0 / temperature);
}

p_from_v_e() [1/3]

void FlibeFluidProperties::p_from_v_e ( const DualReal &  v, const DualReal &  e, DualReal &  p, DualReal &  dp_dv, DualReal &  dp_de  ) const

overridevirtual

Definition at line 76 of file FlibeFluidProperties.C.

{
  p = SinglePhaseFluidProperties::p_from_v_e(v, e);
 
  // chain rule, (dp_de)_v = (dp_dT)_v * (dT_de)_v
  DualReal T, dT_dv, dT_de;
  T_from_v_e(v, e, T, dT_dv, dT_de);
  dp_de = _dp_dT_at_constant_v * dT_de;
 
  // cyclic relation, (dP_dv)_e = - (dp_de)_v * (de_dv)_p
  auto cp = SinglePhaseFluidProperties::cp_from_v_e(v, e);
  auto dT_dv_at_constant_p = -1.0 / (_drho_dT * v * v);
  auto de_dv_at_constant_p = cp * dT_dv_at_constant_p - p;
  dp_dv = -dp_de * de_dv_at_constant_p;
}

p_from_v_e() [2/3]

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

overridevirtual

Pressure from specific volume and specific internal energy.

Parameters

[in]	v	specific volume (m$^3$/kg)
[in]	e	specific internal energy (J/kg)

Returns

pressure (Pa)

Definition at line 52 of file FlibeFluidProperties.C.

{
  Real temperature = T_from_v_e(v, e);
  return (1.0 / v - _drho_dT * temperature - _c0) / _drho_dp + _p_atm;
}

Referenced by p_from_v_e(), and T_from_v_e().

p_from_v_e() [3/3]

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

overridevirtual

Pressure and its derivatives from specific volume and specific internal energy.

Parameters

[in]	v	specific volume (m$^3$/kg)
[in]	e	specific internal energy (J/kg)
[out]	p	pressure (Pa)
[out]	dp_dv	derivative of pressure w.r.t. specific volume
[out]	dp_de	derivative of pressure w.r.t. specific internal energy

Definition at line 59 of file FlibeFluidProperties.C.

{
  p = p_from_v_e(v, e);
 
  // chain rule, (dp_de)_v = (dp_dT)_v * (dT_de)_v
  Real T, dT_dv, dT_de;
  T_from_v_e(v, e, T, dT_dv, dT_de);
  dp_de = _dp_dT_at_constant_v * dT_de;
 
  // cyclic relation, (dP_dv)_e = - (dp_de)_v * (de_dv)_p
  Real cp = cp_from_v_e(v, e);
  Real dT_dv_at_constant_p = -1.0 / (_drho_dT * v * v);
  Real de_dv_at_constant_p = cp * dT_dv_at_constant_p - p;
  dp_dv = -dp_de * de_dv_at_constant_p;
}

propfunc() [1/16]

e e e e p h T T SinglePhaseFluidProperties::propfunc ( c  , p  , T    )

inherited

propfunc() [2/16]

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

inherited

propfunc() [3/16]

e e e e p h T T T SinglePhaseFluidProperties::propfunc ( cv  , p  , T    )

inherited

propfunc() [4/16]

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

inherited

propfunc() [5/16]

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

inherited

propfunc() [6/16]

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

inherited

propfunc() [7/16]

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

inherited

propfunc() [8/16]

e e e e p h T T T T SinglePhaseFluidProperties::propfunc ( k  , p  , T    )

inherited

propfunc() [9/16]

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

inherited

propfunc() [10/16]

e e e e p h T SinglePhaseFluidProperties::propfunc ( mu  , rho  , T    )

inherited

propfunc() [11/16]

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

inherited

propfunc() [12/16]

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:

@begincode 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] gamma Adiabatic ratio (cp/cv) [-]

As an example:

@begincode // 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) and x_from_a_b(DualReal a, DualReal b, DualReal x, DualReal dx_da, DualReal dx_db) versions of the functions where a and b must be ADReal/DualNumber's calculated using all AD-supporting values:

@begincode 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() [13/16]

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

inherited

propfunc() [14/16]

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

inherited

propfunc() [15/16]

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

inherited

propfunc() [16/16]

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

inherited

propfuncWithDefault() [1/2]

e e e e p h T T T T T v v v s h SinglePhaseFluidProperties::propfuncWithDefault ( beta  , p  , T    )

inherited

propfuncWithDefault() [2/2]

e e e e p h T T T T T v v v s h T SinglePhaseFluidProperties::propfuncWithDefault ( e  , p  , T    )

inherited

rho_e_from_p_T()

void SinglePhaseFluidProperties::rho_e_from_p_T ( Real  p, Real  T, Real &  rho, Real &  drho_dp, Real &  drho_dT, Real &  e, Real &  de_dp, Real &  de_dT  ) const

virtualinherited

Definition at line 242 of file SinglePhaseFluidProperties.C.

{
  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_T() [1/3]

void FlibeFluidProperties::rho_from_p_T ( const DualReal &  p, const DualReal &  T, DualReal &  rho, DualReal &  drho_dp, DualReal &  drho_dT  ) const

overridevirtual

Definition at line 214 of file FlibeFluidProperties.C.

{
  rho = SinglePhaseFluidProperties::rho_from_p_T(pressure, temperature);
  drho_dp = _drho_dp;
  drho_dT = _drho_dT;
}

rho_from_p_T() [2/3]

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

overridevirtual

Density from pressure and temperature.

Parameters

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

Returns

density (kg/m$^3$)

Definition at line 199 of file FlibeFluidProperties.C.

{
  return _drho_dT * temperature + _drho_dp * (pressure - _p_atm) + _c0;
}

Referenced by rho_from_p_T().

rho_from_p_T() [3/3]

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

overridevirtual

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 205 of file FlibeFluidProperties.C.

{
  rho = rho_from_p_T(pressure, temperature);
  drho_dp = _drho_dp;
  drho_dT = _drho_dT;
}

rho_mu_from_p_T() [1/3]

void SinglePhaseFluidProperties::rho_mu_from_p_T ( const DualReal &  p, const DualReal &  T, DualReal &  rho, DualReal &  mu  ) const

virtualinherited

Definition at line 277 of file SinglePhaseFluidProperties.C.

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

rho_mu_from_p_T() [2/3]

void SinglePhaseFluidProperties::rho_mu_from_p_T ( Real  p, Real  T, Real &  rho, Real &  drho_dp, Real &  drho_dT, Real &  mu, Real &  dmu_dp, Real &  dmu_dT  ) const

virtualinherited

Reimplemented in Water97FluidProperties, CO2FluidProperties, HydrogenFluidProperties, and NitrogenFluidProperties.

Definition at line 263 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);
}

rho_mu_from_p_T() [3/3]

void SinglePhaseFluidProperties::rho_mu_from_p_T ( Real  p, Real  T, Real &  rho, Real &  mu  ) const

virtualinherited

Combined methods.

These methods are particularly useful for the PorousFlow module, where density and viscosity are typically both computed everywhere. The combined methods allow the most efficient means of calculating both properties, especially where rho(p, T) and mu(rho, T). In this case, an extra density calculation would be required to calculate mu(p, T). All propery names are described above.

Reimplemented in Water97FluidProperties, CO2FluidProperties, HydrogenFluidProperties, and NitrogenFluidProperties.

Definition at line 256 of file SinglePhaseFluidProperties.C.

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

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

subdomainSetup()

virtual void FluidProperties::subdomainSetup ( )

inlinefinalvirtualinherited

Definition at line 39 of file FluidProperties.h.

{}

T_from_v_e() [1/3]

void FlibeFluidProperties::T_from_v_e ( const DualReal &  v, const DualReal &  e, DualReal &  T, DualReal &  dT_dv, DualReal &  dT_de  ) const

overridevirtual

Definition at line 130 of file FlibeFluidProperties.C.

{
  T = SinglePhaseFluidProperties::T_from_v_e(v, e);
 
  // reciprocity relation based on the definition of cv
  auto cv = SinglePhaseFluidProperties::cv_from_v_e(v, e);
  dT_de = 1.0 / cv;
 
  // cyclic relation, (dT_dv)_e = -(dT_de)_v * (de_dv)_T
  auto p = SinglePhaseFluidProperties::p_from_v_e(v, e);
  auto dp_dv_at_constant_T = -1.0 / (_drho_dp * v * v);
  auto de_dv_at_constant_T = -(p + v * dp_dv_at_constant_T);
  dT_dv = -dT_de * de_dv_at_constant_T;
}

T_from_v_e() [2/3]

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

overridevirtual

Temperature from specific volume and specific internal energy.

Parameters

[in]	v	specific volume (m$^3$/kg)
[in]	e	specific internal energy (J/kg)

Returns

temperature (K)

Definition at line 94 of file FlibeFluidProperties.C.

{
  // We need to write these in a somewhat strange manner to ensure that pressure
  // and temperature do not depend implicitly on each other, causing a circular
  // logic problem. Substituting the definition for pressure based on the
  // rho * (h - e) = P, where h = Cp * T into the density correlation for flibe,
  // we can rearrange and get temperature in terms of only v and e
 
  // p = (Cp * T - e) / v
  // T = (1 / v - drho_dp * [p                - p_atm] + _c0) / drho_dT
  //   = (1 / v - drho_dp * [(Cp * T - e) / v - p_atm] + _c0) / drho_dT
  //   = (1 + drho_dp * e + p_atm * v * drho_dp - _c0 * v) / (drho_dT * v + drho_dp * Cp)
 
  Real cp = cp_from_v_e(v, e);
  Real numerator = 1.0 + _drho_dp * (e + _p_atm * v) - _c0 * v;
  Real denominator = _drho_dT * v + _drho_dp * cp;
  return numerator / denominator;
}

Referenced by k_from_v_e(), mu_from_v_e(), p_from_v_e(), and T_from_v_e().

T_from_v_e() [3/3]

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

overridevirtual

Temperature and its derivatives from specific volume and specific internal energy.

Parameters

[in]	v	specific volume (m$^3$/kg)
[in]	e	specific internal energy (J/kg)
[out]	T	temperature (K)
[out]	dT_dv	derivative of temperature w.r.t. specific volume
[out]	dT_de	derivative of temperature w.r.t. specific internal energy

Definition at line 114 of file FlibeFluidProperties.C.

{
  T = T_from_v_e(v, e);
 
  // reciprocity relation based on the definition of cv
  Real cv = cv_from_v_e(v, e);
  dT_de = 1.0 / cv;
 
  // cyclic relation, (dT_dv)_e = -(dT_de)_v * (de_dv)_T
  Real p = p_from_v_e(v, e);
  Real dp_dv_at_constant_T = -1.0 / (_drho_dp * v * v);
  Real de_dv_at_constant_T = -(p + v * dp_dv_at_constant_T);
  dT_dv = -dT_de * de_dv_at_constant_T;
}

threadJoin()

virtual void FluidProperties::threadJoin ( const UserObject &  )

inlinefinalvirtualinherited

Definition at line 38 of file FluidProperties.h.

{}

triplePointPressure()

Real SinglePhaseFluidProperties::triplePointPressure ( ) const

virtualinherited

Triple point pressure.

Returns

triple point pressure (Pa)

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

Definition at line 132 of file SinglePhaseFluidProperties.C.

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

triplePointTemperature()

Real SinglePhaseFluidProperties::triplePointTemperature ( ) const

virtualinherited

Triple point temperature.

Returns

triple point temperature (K)

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

Definition at line 138 of file SinglePhaseFluidProperties.C.

{
  mooseError(name(), ": ", __PRETTY_FUNCTION__, " 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 IdealGasFluidProperties, and StiffenedGasFluidProperties.

Definition at line 292 of file SinglePhaseFluidProperties.C.

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

Referenced by IdealRealGasMixtureFluidProperties::v_from_p_T().

v_from_p_T() [1/3]

DualReal FlibeFluidProperties::v_from_p_T ( const DualReal &  p, const DualReal &  T  ) const

overridevirtual

Definition at line 226 of file FlibeFluidProperties.C.

{
  return 1.0 / (_drho_dT * temperature + _drho_dp * (pressure - _p_atm) + _c0);
}

v_from_p_T() [2/3]

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

overridevirtual

Specific volume from pressure and temperature.

Parameters

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

Returns

specific volume (m$^3$/kg)

Definition at line 232 of file FlibeFluidProperties.C.

{
  return 1.0 / (_drho_dT * temperature + _drho_dp * (pressure - _p_atm) + _c0);
}

Referenced by cv_from_p_T(), e_from_p_T(), and v_from_p_T().

v_from_p_T() [3/3]

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

overridevirtual

Specific volume and its derivatives from pressure and temperature.

Parameters

[in]	p	pressure (Pa)
[in]	T	temperature (K)
[out]	v	specific volume (m$^3$/kg)
[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 238 of file FlibeFluidProperties.C.

{
  v = v_from_p_T(pressure, temperature);
  dv_dp = -v * v * _drho_dp;
  dv_dT = -v * v * _drho_dT;
}

vaporPressure() [1/3]

DualReal SinglePhaseFluidProperties::vaporPressure ( const DualReal &  T ) const

inherited

Definition at line 198 of file SinglePhaseFluidProperties.C.

{
  Real p = 0.0;
  Real temperature = T.value();
  Real dpdT = 0.0;
 
  vaporPressure(temperature, p, dpdT);
 
  DualReal result = p;
  result.derivatives() = T.derivatives() * dpdT;
 
  return result;
}

vaporPressure() [2/3]

Real SinglePhaseFluidProperties::vaporPressure ( Real  T ) const

virtualinherited

Vapor pressure.

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

Parameters

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

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

Definition at line 177 of file SinglePhaseFluidProperties.C.

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

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

vaporPressure() [3/3]

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

virtualinherited

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

Definition at line 189 of file SinglePhaseFluidProperties.C.

{
  fluidPropError(name(), ": ", __PRETTY_FUNCTION__, " derivatives not implemented.");
 
  dp_dT = 0.0;
  p = vaporPressure(T);
}

vaporTemperature() [1/3]

DualReal SinglePhaseFluidProperties::vaporTemperature ( const DualReal &  p ) const

inherited

Definition at line 227 of file SinglePhaseFluidProperties.C.

{
  Real T = 0.0;
  Real pressure = p.value();
  Real dTdp = 0.0;
 
  vaporTemperature(pressure, T, dTdp);
 
  DualReal result = T;
  result.derivatives() = p.derivatives() * dTdp;
 
  return result;
}

vaporTemperature() [2/3]

Real SinglePhaseFluidProperties::vaporTemperature ( Real  p ) const

virtualinherited

Vapor temperature.

Used to delineate liquid and gas phases. Valid for pressures between the triple point pressure and the critical pressure

Parameters

	p	fluid pressure (Pa)
[out]	saturation	temperature (K)
[out]	derivative	of saturation temperature wrt pressure

Reimplemented in Water97FluidProperties.

Definition at line 212 of file SinglePhaseFluidProperties.C.

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

Referenced by PorousFlowWaterVapor::thermophysicalProperties(), and SinglePhaseFluidProperties::vaporTemperature().

vaporTemperature() [3/3]

void SinglePhaseFluidProperties::vaporTemperature ( Real  p, Real &  Tsat, Real &  dTsat_dp  ) const

virtualinherited

Reimplemented in Water97FluidProperties.

Definition at line 218 of file SinglePhaseFluidProperties.C.

{
  fluidPropError(name(), ": ", __PRETTY_FUNCTION__, " derivatives not implemented.");
 
  dT_dp = 0.0;
  T = vaporTemperature(p);
}

Member Data Documentation

_allow_imperfect_jacobians

const bool FluidProperties::_allow_imperfect_jacobians

protectedinherited

Flag to set unimplemented Jacobian entries to zero.

Definition at line 48 of file FluidProperties.h.

Referenced by SinglePhaseFluidProperties::fluidPropError().

_c0

const Real FlibeFluidProperties::_c0

protected

additive constant to rho(P, T) correlation

Definition at line 334 of file FlibeFluidProperties.h.

Referenced by p_from_v_e(), rho_from_p_T(), T_from_v_e(), and v_from_p_T().

_cp

const Real FlibeFluidProperties::_cp

protected

specific heat at constant pressure

Definition at line 331 of file FlibeFluidProperties.h.

Referenced by cp_from_p_T(), and cp_from_v_e().

_dp_dT_at_constant_v

const Real FlibeFluidProperties::_dp_dT_at_constant_v

protected

derivative of pressure with respect to temperature at constant specific volume

Definition at line 337 of file FlibeFluidProperties.h.

Referenced by cv_from_v_e(), and p_from_v_e().

_drho_dp

const Real& FlibeFluidProperties::_drho_dp

protected

Derivative of density with respect to pressure at fixed temperature.

Definition at line 322 of file FlibeFluidProperties.h.

Referenced by p_from_v_e(), rho_from_p_T(), T_from_v_e(), and v_from_p_T().

_drho_dT

const Real FlibeFluidProperties::_drho_dT

protected

Derivative of density with respect to temperature at fixed pressure.

Definition at line 325 of file FlibeFluidProperties.h.

Referenced by p_from_v_e(), rho_from_p_T(), T_from_v_e(), and v_from_p_T().

_p_atm

const Real FlibeFluidProperties::_p_atm

protected

Atmospheric pressure, Pa.

Definition at line 328 of file FlibeFluidProperties.h.

Referenced by p_from_v_e(), rho_from_p_T(), T_from_v_e(), and v_from_p_T().

_R

const Real FluidProperties::_R = 8.3144598

staticinherited

Universal gas constant (J/mol/K)

Definition at line 42 of file FluidProperties.h.

Referenced by HelmholtzFluidProperties::c_from_p_T(), IdealGasFluidProperties::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(), IdealGasFluidProperties::rho_from_p_T(), and HelmholtzFluidProperties::s_from_p_T().

_T_c2k

const Real FluidProperties::_T_c2k

protectedinherited

Conversion of temperature from Celsius to Kelvin.

Definition at line 46 of file FluidProperties.h.

Referenced by NaClFluidProperties::cp_from_p_T(), BrineFluidProperties::cp_from_p_T_X(), NaClFluidProperties::h_from_p_T(), BrineFluidProperties::h_from_p_T_X(), BrineFluidProperties::haliteSolubility(), NaClFluidProperties::k_from_p_T(), BrineFluidProperties::k_from_p_T_X(), BrineFluidProperties::mu_from_p_T_X(), CO2FluidProperties::partialDensity(), NaClFluidProperties::rho_from_p_T(), and BrineFluidProperties::rho_from_p_T_X().

h [1/2]

e e e e SinglePhaseFluidProperties::h

inherited

Definition at line 163 of file SinglePhaseFluidProperties.h.

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

h [2/2]

e e e e p h T T T T T v v v SinglePhaseFluidProperties::h

inherited

Definition at line 183 of file SinglePhaseFluidProperties.h.

p [1/6]

e e e e p h SinglePhaseFluidProperties::p

inherited

Definition at line 167 of file SinglePhaseFluidProperties.h.

Referenced by StiffenedGasFluidProperties::c_from_v_e(), HeliumFluidProperties::c_from_v_e(), IdealGasFluidProperties::cp_from_p_T(), IdealGasFluidProperties::cv_from_p_T(), StiffenedGasFluidProperties::e_from_p_rho(), IdealGasFluidProperties::e_from_p_rho(), StiffenedGasFluidProperties::e_from_p_T(), IdealGasFluidProperties::e_from_p_T(), StiffenedGasFluidProperties::g_from_v_e(), IdealGasFluidProperties::g_from_v_e(), TabulatedFluidProperties::generateTabulatedData(), StiffenedGasFluidProperties::h_from_p_T(), IdealGasFluidProperties::h_from_p_T(), Water97FluidProperties::henryConstant(), IdealGasFluidProperties::k_from_p_T(), StiffenedGasFluidProperties::p_from_h_s(), IdealGasFluidProperties::p_from_h_s(), StiffenedGasFluidProperties::p_from_T_v(), IdealGasFluidProperties::p_from_T_v(), IdealGasFluidProperties::p_from_v_e(), StiffenedGasFluidProperties::p_from_v_e(), HeliumFluidProperties::p_from_v_e(), FlinakFluidProperties::p_from_v_e(), p_from_v_e(), SinglePhaseFluidProperties::rho_e_from_p_T(), StiffenedGasFluidProperties::rho_from_p_s(), IdealGasFluidProperties::rho_from_p_s(), StiffenedGasFluidProperties::rho_from_p_T(), IdealGasFluidProperties::rho_from_p_T(), SinglePhaseFluidProperties::rho_mu_from_p_T(), StiffenedGasFluidProperties::s_from_h_p(), IdealGasFluidProperties::s_from_h_p(), StiffenedGasFluidProperties::s_from_p_T(), IdealGasFluidProperties::s_from_p_T(), SimpleFluidProperties::s_from_p_T(), Water97FluidProperties::s_from_p_T(), TabulatedFluidProperties::s_from_p_T(), IdealGasFluidProperties::s_from_T_v(), StiffenedGasFluidProperties::s_from_v_e(), IdealGasFluidProperties::s_from_v_e(), Water97FluidProperties::T_from_p_h(), FlinakFluidProperties::T_from_v_e(), T_from_v_e(), Water97FluidProperties::vaporPressure(), SinglePhaseFluidProperties::vaporPressure(), Water97FluidProperties::vaporTemperature(), SinglePhaseFluidProperties::vaporTemperature(), and TabulatedFluidProperties::writeTabulatedData().

p [2/6]

e e e e p h T T SinglePhaseFluidProperties::p

inherited

Definition at line 171 of file SinglePhaseFluidProperties.h.

p [3/6]

e e e e p h T T T SinglePhaseFluidProperties::p

inherited

Definition at line 173 of file SinglePhaseFluidProperties.h.

p [4/6]

e e e e p h T T T T SinglePhaseFluidProperties::p

inherited

Definition at line 175 of file SinglePhaseFluidProperties.h.

p [5/6]

e e e e p h T T T T T v v v s SinglePhaseFluidProperties::p

inherited

Definition at line 185 of file SinglePhaseFluidProperties.h.

p [6/6]

e e e e p h T T T T T v v v s h SinglePhaseFluidProperties::p

inherited

Definition at line 187 of file SinglePhaseFluidProperties.h.

propfuncWithDefault

e e e e p h T T T T T v v v s h T e SinglePhaseFluidProperties::propfuncWithDefault(gamma, p, T)

inherited

Definition at line 190 of file SinglePhaseFluidProperties.h.

rho

e e e e p h T SinglePhaseFluidProperties::rho

inherited

Definition at line 169 of file SinglePhaseFluidProperties.h.

Referenced by HeliumFluidProperties::beta_from_p_T(), FlinakFluidProperties::beta_from_p_T(), StiffenedGasFluidProperties::c2_from_p_rho(), HeliumFluidProperties::c_from_v_e(), StiffenedGasFluidProperties::e_from_p_rho(), IdealGasFluidProperties::e_from_p_rho(), NaClFluidProperties::e_from_p_T(), Water97FluidProperties::k_from_p_T(), CO2FluidProperties::mu_from_p_T(), NitrogenFluidProperties::mu_from_p_T(), HydrogenFluidProperties::mu_from_p_T(), Water97FluidProperties::mu_from_p_T(), SinglePhaseFluidProperties::rho_e_from_p_T(), StiffenedGasFluidProperties::rho_from_p_s(), IdealGasFluidProperties::rho_from_p_s(), HelmholtzFluidProperties::rho_from_p_T(), StiffenedGasFluidProperties::rho_from_p_T(), CO2FluidProperties::rho_from_p_T(), Water97FluidProperties::rho_from_p_T(), NaClFluidProperties::rho_from_p_T(), IdealGasFluidProperties::rho_from_p_T(), SimpleFluidProperties::rho_from_p_T(), TabulatedFluidProperties::rho_from_p_T(), FlinakFluidProperties::rho_from_p_T(), rho_from_p_T(), HeliumFluidProperties::rho_from_p_T(), NitrogenFluidProperties::rho_mu_from_p_T(), HydrogenFluidProperties::rho_mu_from_p_T(), CO2FluidProperties::rho_mu_from_p_T(), Water97FluidProperties::rho_mu_from_p_T(), and SinglePhaseFluidProperties::rho_mu_from_p_T().

T [1/3]

e e e e p h T T T T T SinglePhaseFluidProperties::T

inherited

Definition at line 177 of file SinglePhaseFluidProperties.h.

Referenced by IdealGasFluidProperties::c_from_p_T(), IdealGasFluidProperties::c_from_v_e(), HeliumFluidProperties::c_from_v_e(), IdealGasFluidProperties::cp_from_p_T(), IdealGasFluidProperties::cv_from_p_T(), StiffenedGasFluidProperties::e_from_p_T(), IdealGasFluidProperties::e_from_p_T(), StiffenedGasFluidProperties::e_from_T_v(), IdealGasFluidProperties::e_from_T_v(), StiffenedGasFluidProperties::g_from_v_e(), IdealGasFluidProperties::g_from_v_e(), StiffenedGasFluidProperties::h_from_p_T(), IdealGasFluidProperties::h_from_p_T(), StiffenedGasFluidProperties::h_from_T_v(), IdealGasFluidProperties::h_from_T_v(), Water97FluidProperties::henryConstant(), IdealGasFluidProperties::k_from_p_T(), HeliumFluidProperties::k_from_v_e(), IdealGasFluidProperties::mu_from_p_T(), StiffenedGasFluidProperties::p_from_T_v(), IdealGasFluidProperties::p_from_T_v(), HeliumFluidProperties::p_from_v_e(), p_from_v_e(), FlinakFluidProperties::p_from_v_e(), SinglePhaseFluidProperties::rho_e_from_p_T(), StiffenedGasFluidProperties::rho_from_p_s(), IdealGasFluidProperties::rho_from_p_s(), StiffenedGasFluidProperties::rho_from_p_T(), IdealGasFluidProperties::rho_from_p_T(), SinglePhaseFluidProperties::rho_mu_from_p_T(), StiffenedGasFluidProperties::s_from_p_T(), IdealGasFluidProperties::s_from_p_T(), SimpleFluidProperties::s_from_p_T(), Water97FluidProperties::s_from_p_T(), TabulatedFluidProperties::s_from_p_T(), StiffenedGasFluidProperties::s_from_T_v(), IdealGasFluidProperties::s_from_T_v(), StiffenedGasFluidProperties::s_from_v_e(), IdealGasFluidProperties::s_from_v_e(), IdealGasFluidProperties::T_from_p_h(), Water97FluidProperties::T_from_p_h(), StiffenedGasFluidProperties::T_from_v_e(), IdealGasFluidProperties::T_from_v_e(), T_from_v_e(), FlinakFluidProperties::T_from_v_e(), HeliumFluidProperties::T_from_v_e(), SinglePhaseFluidProperties::vaporPressure(), Water97FluidProperties::vaporTemperature(), and SinglePhaseFluidProperties::vaporTemperature().

T [2/3]

e e e e p h T T T T T v SinglePhaseFluidProperties::T

inherited

Definition at line 179 of file SinglePhaseFluidProperties.h.

T [3/3]

e e e e p h T T T T T v v SinglePhaseFluidProperties::T

inherited

Definition at line 181 of file SinglePhaseFluidProperties.h.

v [1/6]

SinglePhaseFluidProperties::v

inherited

Definition at line 155 of file SinglePhaseFluidProperties.h.

Referenced by StiffenedGasFluidProperties::c_from_v_e(), IdealGasFluidProperties::c_from_v_e(), HeliumFluidProperties::c_from_v_e(), StiffenedGasFluidProperties::cp_from_v_e(), IdealGasFluidProperties::cp_from_v_e(), cp_from_v_e(), FlinakFluidProperties::cp_from_v_e(), HeliumFluidProperties::cp_from_v_e(), cv_from_p_T(), FlinakFluidProperties::cv_from_p_T(), IdealGasFluidProperties::cv_from_v_e(), cv_from_v_e(), FlinakFluidProperties::cv_from_v_e(), HeliumFluidProperties::cv_from_v_e(), e_from_p_T(), FlinakFluidProperties::e_from_p_T(), StiffenedGasFluidProperties::e_from_T_v(), IdealGasFluidProperties::e_from_v_h(), StiffenedGasFluidProperties::e_from_v_h(), StiffenedGasFluidProperties::g_from_v_e(), IdealGasFluidProperties::g_from_v_e(), k_from_v_e(), FlinakFluidProperties::k_from_v_e(), HeliumFluidProperties::k_from_v_e(), mu_from_v_e(), FlinakFluidProperties::mu_from_v_e(), HeliumFluidProperties::mu_from_v_e(), StiffenedGasFluidProperties::p_from_T_v(), IdealGasFluidProperties::p_from_T_v(), IdealGasFluidProperties::p_from_v_e(), StiffenedGasFluidProperties::p_from_v_e(), HeliumFluidProperties::p_from_v_e(), p_from_v_e(), FlinakFluidProperties::p_from_v_e(), StiffenedGasFluidProperties::s_from_T_v(), IdealGasFluidProperties::s_from_T_v(), StiffenedGasFluidProperties::s_from_v_e(), IdealGasFluidProperties::s_from_v_e(), StiffenedGasFluidProperties::T_from_v_e(), IdealGasFluidProperties::T_from_v_e(), FlinakFluidProperties::T_from_v_e(), T_from_v_e(), HeliumFluidProperties::T_from_v_e(), StiffenedGasFluidProperties::v_e_spndl_from_T(), IdealGasFluidProperties::v_e_spndl_from_T(), v_from_p_T(), and FlinakFluidProperties::v_from_p_T().

v [2/6]

e SinglePhaseFluidProperties::v

inherited

Definition at line 157 of file SinglePhaseFluidProperties.h.

v [3/6]

e e SinglePhaseFluidProperties::v

inherited

Definition at line 159 of file SinglePhaseFluidProperties.h.

v [4/6]

e e e SinglePhaseFluidProperties::v

inherited

Definition at line 161 of file SinglePhaseFluidProperties.h.

v [5/6]

e e e e p SinglePhaseFluidProperties::v

inherited

Definition at line 165 of file SinglePhaseFluidProperties.h.

v [6/6]

e e e e p h T T T T T v v v s h T SinglePhaseFluidProperties::v

inherited

Definition at line 189 of file SinglePhaseFluidProperties.h.

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

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