NaClFluidProperties Class Reference

NaCl fluid properties as a function of pressure (Pa) and temperature (K). More...

#include <NaClFluidProperties.h>

Inheritance diagram for NaClFluidProperties:

Public Member Functions
	NaClFluidProperties (const InputParameters &parameters)
virtual	~NaClFluidProperties ()
virtual std::string	fluidName () const override
virtual Real	molarMass () const override
	Fluid name. More...
virtual Real	criticalPressure () const override
	Critical pressure. More...
virtual Real	criticalTemperature () const override
	Critical temperature. More...
virtual Real	criticalDensity () const override
	Critical density. More...
virtual Real	triplePointPressure () const override
	Triple point pressure. More...
virtual Real	triplePointTemperature () const override
	Triple point temperature. More...
virtual Real	rho_from_p_T (Real pressure, Real temperature) const override
virtual void	rho_from_p_T (Real pressure, Real temperature, Real &rho, Real &drho_dp, Real &drho_dT) const override
virtual Real	e_from_p_T (Real pressure, Real temperature) const override
virtual void	e_from_p_T (Real pressure, Real temperature, Real &e, Real &de_dp, Real &de_dT) const override
virtual Real	cp_from_p_T (Real pressure, Real temperature) const override
virtual Real	cv_from_p_T (Real pressure, Real temperature) 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	h_from_p_T (Real pressure, Real temperature) const override
virtual void	h_from_p_T (Real pressure, Real temperature, Real &h, Real &dh_dp, Real &dh_dT) const override
virtual Real	criticalInternalEnergy () const
	Critical specific internal energy. 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	_Mnacl
	NaCl molar mass (kg/mol) More...
const Real	_p_critical
	Critical pressure (Pa) More...
const Real	_T_critical
	Critical temperature (K) More...
const Real	_rho_critical
	Critical density (kg/m^3) More...
const Real	_p_triple
	Triple point pressure (Pa) More...
const Real	_T_triple
	Triple point temperature (K) 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

NaCl fluid properties as a function of pressure (Pa) and temperature (K).

Note: only solid state (halite) properties are currently implemented to use in brine formulation

Most properties from: Driesner, The system H2O-NaCl. Part II: Correlations for molar volume, enthalpy, and isobaric heat capacity from 0 to 1000 C, 1 to 500 bar, and 0 to 1 Xnacl, Geochimica et Cosmochimica Acta 71, 4902-4919 (2007)

Thermal conductivity from: Urqhart and Bauer, Experimental determination of single-crystal halite thermal conductivity, diffusivity and specific heat from -75 C to 300 C, Int. J. Rock Mech. and Mining Sci., 78 (2015) Note: The function given in this reference doesn't satisfactorily match their experimental data, so the data was refitted using a third order polynomial

NaCl critical properties from: From Anderko and Pitzer, Equation of state for pure sodium chloride, Fluid Phase Equil., 79 (1992)

Definition at line 43 of file NaClFluidProperties.h.

Constructor & Destructor Documentation

NaClFluidProperties()

NaClFluidProperties::NaClFluidProperties

(

const InputParameters &

parameters

)

Definition at line 23 of file NaClFluidProperties.C.

  : SinglePhaseFluidProperties(parameters),
    _Mnacl(58.443e-3),
    _p_critical(1.82e7),
    _T_critical(3841.15),
    _rho_critical(108.43),
    _p_triple(50.0),
    _T_triple(1073.85)
{
}

~NaClFluidProperties()

NaClFluidProperties::~NaClFluidProperties ( )

virtual

Definition at line 34 of file NaClFluidProperties.C.

{}

Member Function Documentation

cp_from_p_T()

Real NaClFluidProperties::cp_from_p_T ( Real  pressure, Real  temperature  ) const

overridevirtual

Definition at line 137 of file NaClFluidProperties.C.

{
  // Correlation needs pressure in bar
  Real pbar = pressure * 10.0e-5;
  // Correlation requires temperature in Celcius
  Real Tc = temperature - _T_c2k;
  // Triple point temperature of NaCl (in C)
  Real Tt = _T_triple - _T_c2k;
  // Coefficients used in the correlation
  Real r3 = -1.7099e-3 - 3.82734e-6 * Tc - 8.65455e-9 * Tc * Tc;
  Real r4 = 5.29063e-8 - 9.63084e-11 * Tc + 6.50745e-13 * Tc * Tc;
 
  // Halite isobaric heat capapcity
  return 1148.81 + 0.551548 * (Tc - Tt) + 2.64309e-4 * (Tc - Tt) * (Tc - Tt) + r3 * pbar +
         r4 * pbar * pbar;
}

criticalDensity()

Real NaClFluidProperties::criticalDensity ( ) const

overridevirtual

Critical density.

Returns

critical density (kg/m^3)

Reimplemented from SinglePhaseFluidProperties.

Definition at line 61 of file NaClFluidProperties.C.

{
  return _rho_critical;
}

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 NaClFluidProperties::criticalPressure ( ) const

overridevirtual

Critical pressure.

Returns

critical pressure (Pa)

Reimplemented from SinglePhaseFluidProperties.

Definition at line 49 of file NaClFluidProperties.C.

{
  return _p_critical;
}

criticalTemperature()

Real NaClFluidProperties::criticalTemperature ( ) const

overridevirtual

Critical temperature.

Returns

critical temperature (K)

Reimplemented from SinglePhaseFluidProperties.

Definition at line 55 of file NaClFluidProperties.C.

{
  return _T_critical;
}

cv_from_p_T()

Real NaClFluidProperties::cv_from_p_T ( Real  pressure, Real  temperature  ) const

overridevirtual

Definition at line 155 of file NaClFluidProperties.C.

{
  return e_from_p_T(pressure, temperature) / temperature;
}

e_from_p_T() [1/2]

Real NaClFluidProperties::e_from_p_T ( Real  pressure, Real  temperature  ) const

overridevirtual

Definition at line 117 of file NaClFluidProperties.C.

{
  return h_from_p_T(pressure, temperature) - pressure / rho_from_p_T(pressure, temperature);
}

Referenced by cv_from_p_T().

e_from_p_T() [2/2]

void NaClFluidProperties::e_from_p_T ( Real  pressure, Real  temperature, Real &  e, Real &  de_dp, Real &  de_dT  ) const

overridevirtual

Definition at line 123 of file NaClFluidProperties.C.

{
  Real h, dh_dp, dh_dT;
  h_from_p_T(pressure, temperature, h, dh_dp, dh_dT);
  Real rho, drho_dp, drho_dT;
  rho_from_p_T(pressure, temperature, rho, drho_dp, drho_dT);
 
  e = h - pressure / rho;
  de_dp = dh_dp + pressure * drho_dp / rho / rho - 1.0 / rho;
  de_dT = dh_dT + pressure * drho_dT / rho / rho;
}

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 NaClFluidProperties::fluidName ( ) const

overridevirtual

Definition at line 37 of file NaClFluidProperties.C.

{
  return "nacl";
}

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 NaClFluidProperties::h_from_p_T ( Real  pressure, Real  temperature  ) const

overridevirtual

Definition at line 182 of file NaClFluidProperties.C.

{
  // Correlation needs pressure in bar
  Real pbar = pressure * 1.0e-5;
  // Correlation requires temperature in Celcius
  Real Tc = temperature - _T_c2k;
  // Triple point temperature of water (in C)
  Real Tt = 273.16 - _T_c2k;
  // Triple point presure of water (in bar)
  Real pt = 611.657 * 1.0e-5;
 
  // Note: the enthalpy of halite is 0 at the triple point of water
  return 8.7664e2 * (Tc - Tt) + 6.4139e-2 * (Tc * Tc - Tt * Tt) +
         8.8101e-5 * (Tc * Tc * Tc - Tt * Tt * Tt) + 44.14 * (pbar - pt);
}

Referenced by e_from_p_T().

h_from_p_T() [2/2]

void NaClFluidProperties::h_from_p_T ( Real  pressure, Real  temperature, Real &  h, Real &  dh_dp, Real &  dh_dT  ) const

overridevirtual

Definition at line 199 of file NaClFluidProperties.C.

{
  // Correlation needs pressure in bar
  Real pbar = pressure * 1.0e-5;
  // Correlation requires temperature in Celcius
  Real Tc = temperature - _T_c2k;
  // Triple point temperature of water (in C)
  Real Tt = 273.16 - _T_c2k;
  // Triple point presure of water (in bar)
  Real pt = 611.657 * 1.0e-5;
 
  // Note: the enthalpy of halite is 0 at the triple point of water
  h = 8.7664e2 * (Tc - Tt) + 6.4139e-2 * (Tc * Tc - Tt * Tt) +
      8.8101e-5 * (Tc * Tc * Tc - Tt * Tt * Tt) + 44.14 * (pbar - pt);
 
  dh_dp = 44.14 * 1.0e-5;
  dh_dT = 8.7664e2 + 2.0 * 6.4139e-2 * Tc + 3.0 * 8.8101e-5 * Tc * Tc;
}

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

overridevirtual

Definition at line 161 of file NaClFluidProperties.C.

{
  // Correlation requires temperature in Celcius
  Real Tc = temperature - _T_c2k;
 
  return 6.82793 - 3.16584e-2 * Tc + 1.03451e-4 * Tc * Tc - 1.48207e-7 * Tc * Tc * Tc;
}

k_from_p_T() [2/2]

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

overridevirtual

Definition at line 170 of file NaClFluidProperties.C.

{
  // Correlation requires temperature in Celcius
  Real Tc = temperature - _T_c2k;
 
  k = 6.82793 - 3.16584e-2 * Tc + 1.03451e-4 * Tc * Tc - 1.48207e-7 * Tc * Tc * Tc;
  dk_dp = 0.0;
  dk_dT = -3.16584e-2 + 2.06902e-4 * Tc - 4.44621e-7 * Tc * Tc;
}

molarMass()

Real NaClFluidProperties::molarMass ( ) const

overridevirtual

Fluid name.

Returns

string representing fluid name Molar mass [kg/mol]

molar mass

Reimplemented from SinglePhaseFluidProperties.

Definition at line 43 of file NaClFluidProperties.C.

{
  return _Mnacl;
}

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() [1/2]

Real NaClFluidProperties::rho_from_p_T ( Real  pressure, Real  temperature  ) const

overridevirtual

Definition at line 79 of file NaClFluidProperties.C.

{
  // Correlation needs pressure in bar
  Real pbar = pressure * 1.0e-5;
  // Correlation requires temperature in Celcius
  Real Tc = temperature - _T_c2k;
 
  // Halite density at 0 Pa
  Real density_P0 = 2.17043e3 - 2.4599e-1 * Tc - 9.5797e-5 * Tc * Tc;
 
  // Halite density as a function of pressure
  Real l = 5.727e-3 + 2.715e-3 * std::exp(Tc / 733.4);
 
  return density_P0 + l * pbar;
}

Referenced by e_from_p_T(), and rho_from_p_T().

rho_from_p_T() [2/2]

void NaClFluidProperties::rho_from_p_T ( Real  pressure, Real  temperature, Real &  rho, Real &  drho_dp, Real &  drho_dT  ) const

overridevirtual

Definition at line 96 of file NaClFluidProperties.C.

{
  rho = this->rho_from_p_T(pressure, temperature);
 
  // Correlation needs pressure in bar
  Real pbar = pressure * 1.0e-5;
  // Correlation requires temperature in Celcius
  Real Tc = temperature - _T_c2k;
 
  // Halite density at 0 Pa
  Real ddensity_P0_dT = -2.4599e-1 - 1.91594e-4 * Tc;
 
  Real l = 5.727e-3 + 2.715e-3 * std::exp(Tc / 733.4);
  Real dl_dT = 2.715e-3 * std::exp(Tc / 733.4) / 733.4;
 
  drho_dp = l * 1.0e-5;
  drho_dT = ddensity_P0_dT + dl_dT * pbar;
}

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.

{}

threadJoin()

virtual void FluidProperties::threadJoin ( const UserObject &  )

inlinefinalvirtualinherited

Definition at line 38 of file FluidProperties.h.

{}

triplePointPressure()

Real NaClFluidProperties::triplePointPressure ( ) const

overridevirtual

Triple point pressure.

Returns

triple point pressure (Pa)

Reimplemented from SinglePhaseFluidProperties.

Definition at line 67 of file NaClFluidProperties.C.

{
  return _p_triple;
}

triplePointTemperature()

Real NaClFluidProperties::triplePointTemperature ( ) const

overridevirtual

Triple point temperature.

Returns

triple point temperature (K)

Reimplemented from SinglePhaseFluidProperties.

Definition at line 73 of file NaClFluidProperties.C.

{
  return _T_triple;
}

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().

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().

_Mnacl

const Real NaClFluidProperties::_Mnacl

protected

NaCl molar mass (kg/mol)

Definition at line 91 of file NaClFluidProperties.h.

Referenced by molarMass().

_p_critical

const Real NaClFluidProperties::_p_critical

protected

Critical pressure (Pa)

Definition at line 93 of file NaClFluidProperties.h.

Referenced by criticalPressure().

_p_triple

const Real NaClFluidProperties::_p_triple

protected

Triple point pressure (Pa)

Definition at line 99 of file NaClFluidProperties.h.

Referenced by triplePointPressure().

_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().

_rho_critical

const Real NaClFluidProperties::_rho_critical

protected

Critical density (kg/m^3)

Definition at line 97 of file NaClFluidProperties.h.

Referenced by criticalDensity().

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

_T_critical

const Real NaClFluidProperties::_T_critical

protected

Critical temperature (K)

Definition at line 95 of file NaClFluidProperties.h.

Referenced by criticalTemperature().

_T_triple

const Real NaClFluidProperties::_T_triple

protected

Triple point temperature (K)

Definition at line 101 of file NaClFluidProperties.h.

Referenced by cp_from_p_T(), and triplePointTemperature().

h [1/2]

e e e e SinglePhaseFluidProperties::h

inherited

Definition at line 163 of file SinglePhaseFluidProperties.h.

Referenced by e_from_p_T(), IdealGasFluidProperties::e_from_v_h(), StiffenedGasFluidProperties::e_from_v_h(), HelmholtzFluidProperties::h_from_p_T(), StiffenedGasFluidProperties::h_from_p_T(), h_from_p_T(), IdealGasFluidProperties::h_from_p_T(), SimpleFluidProperties::h_from_p_T(), Water97FluidProperties::h_from_p_T(), TabulatedFluidProperties::h_from_p_T(), FlibeFluidProperties::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(), FlibeFluidProperties::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(), FlibeFluidProperties::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(), 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(), rho_from_p_T(), IdealGasFluidProperties::rho_from_p_T(), SimpleFluidProperties::rho_from_p_T(), TabulatedFluidProperties::rho_from_p_T(), FlibeFluidProperties::rho_from_p_T(), FlinakFluidProperties::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(), FlibeFluidProperties::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(), FlinakFluidProperties::T_from_v_e(), FlibeFluidProperties::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(), FlibeFluidProperties::cp_from_v_e(), FlinakFluidProperties::cp_from_v_e(), HeliumFluidProperties::cp_from_v_e(), FlibeFluidProperties::cv_from_p_T(), FlinakFluidProperties::cv_from_p_T(), IdealGasFluidProperties::cv_from_v_e(), FlibeFluidProperties::cv_from_v_e(), FlinakFluidProperties::cv_from_v_e(), HeliumFluidProperties::cv_from_v_e(), FlinakFluidProperties::e_from_p_T(), FlibeFluidProperties::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(), FlibeFluidProperties::k_from_v_e(), FlinakFluidProperties::k_from_v_e(), HeliumFluidProperties::k_from_v_e(), FlibeFluidProperties::mu_from_v_e(), FlinakFluidProperties::mu_from_v_e(), HeliumFluidProperties::mu_from_v_e(), StiffenedGasFluidProperties::p_from_T_v(), IdealGasFluidProperties::p_from_T_v(), StiffenedGasFluidProperties::p_from_v_e(), IdealGasFluidProperties::p_from_v_e(), HeliumFluidProperties::p_from_v_e(), FlibeFluidProperties::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(), FlibeFluidProperties::T_from_v_e(), HeliumFluidProperties::T_from_v_e(), StiffenedGasFluidProperties::v_e_spndl_from_T(), IdealGasFluidProperties::v_e_spndl_from_T(), FlinakFluidProperties::v_from_p_T(), and FlibeFluidProperties::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.

---

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

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