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SinglePhaseFluidProperties Class Reference

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

#include <SinglePhaseFluidProperties.h>

Inheritance diagram for SinglePhaseFluidProperties:
[legend]

Public Member Functions

 SinglePhaseFluidProperties (const InputParameters &parameters)
 
virtual ~SinglePhaseFluidProperties ()
 
virtual virtual std Real molarMass () const
 Fluid name. 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 _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
 
 v
 
v
 
e e v
 
e e e v
 
e e e e h
 
e e e e p v
 
e e e e p h p
 
e e e e p h T rho
 
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 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 h
 
e e e e p h T T T T T v v vp
 
e e e e p h T T T T T v v v s h p
 
e e e e p h T T T T T v v v s h T v
 
e e e e p h T T T T T v v v s h TpropfuncWithDefault (gamma, p, T)
 
 propfunc (p, v, e) propfunc(T
 Compute a fluid property given for the state defined by two given properties. More...
 
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 vpropfunc (g, v, e) propfuncWithDefault(T
 
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
 

Detailed Description

Common class for single phase fluid properties.

Definition at line 89 of file SinglePhaseFluidProperties.h.

Constructor & Destructor Documentation

◆ SinglePhaseFluidProperties()

SinglePhaseFluidProperties::SinglePhaseFluidProperties ( const InputParameters &  parameters)

Definition at line 22 of file SinglePhaseFluidProperties.C.

23  : FluidProperties(parameters)
24 {
25 }

◆ ~SinglePhaseFluidProperties()

SinglePhaseFluidProperties::~SinglePhaseFluidProperties ( )
virtual

Definition at line 27 of file SinglePhaseFluidProperties.C.

27 {}

Member Function Documentation

◆ criticalDensity()

Real SinglePhaseFluidProperties::criticalDensity ( ) const
virtual

◆ criticalInternalEnergy()

Real SinglePhaseFluidProperties::criticalInternalEnergy ( ) const
virtual

Critical specific internal energy.

Returns
specific internal energy (J/kg)

Reimplemented in IdealGasFluidProperties, and StiffenedGasFluidProperties.

Definition at line 126 of file SinglePhaseFluidProperties.C.

127 {
128  mooseError(name(), ": ", __PRETTY_FUNCTION__, " not implemented.");
129 }

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

◆ criticalPressure()

Real SinglePhaseFluidProperties::criticalPressure ( ) const
virtual

Critical pressure.

Returns
critical pressure (Pa)

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

Definition at line 108 of file SinglePhaseFluidProperties.C.

109 {
110  mooseError(name(), ": ", __PRETTY_FUNCTION__, " not implemented.");
111 }

◆ criticalTemperature()

Real SinglePhaseFluidProperties::criticalTemperature ( ) const
virtual

◆ e_spndl_from_v()

Real SinglePhaseFluidProperties::e_spndl_from_v ( Real  v) const
virtual

Specific internal energy from temperature and specific volume.

Parameters
[in]Ttemperature
[in]vspecific volume

Reimplemented in IdealGasFluidProperties, and StiffenedGasFluidProperties.

Definition at line 286 of file SinglePhaseFluidProperties.C.

287 {
288  mooseError(name(), ": ", __PRETTY_FUNCTION__, " not implemented.");
289 }

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.

34 {}

◆ finalize()

virtual void FluidProperties::finalize ( )
inlinefinalvirtualinherited

Definition at line 36 of file FluidProperties.h.

36 {}

◆ fluidPropError()

template<typename... Args>
void SinglePhaseFluidProperties::fluidPropError ( Args...  args) const
inlineprivate

Definition at line 326 of file SinglePhaseFluidProperties.h.

327  {
329  mooseDoOnce(mooseWarning(std::forward<Args>(args)...));
330  else
331  mooseError(std::forward<Args>(args)...);
332  }

Referenced by vaporPressure(), and vaporTemperature().

◆ henryCoefficients()

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

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.

184 {
185  mooseError(name(), ": ", __PRETTY_FUNCTION__, " not implemented.");
186 }

Referenced by TabulatedFluidProperties::henryCoefficients().

◆ initialize()

virtual void FluidProperties::initialize ( )
inlinefinalvirtualinherited

Definition at line 35 of file FluidProperties.h.

35 {}

◆ molarMass()

Real SinglePhaseFluidProperties::molarMass ( ) const
virtual

◆ propfunc() [1/16]

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

◆ propfunc() [2/16]

e SinglePhaseFluidProperties::propfunc ( ,
v  ,
 
)

◆ propfunc() [3/16]

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

◆ propfunc() [4/16]

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

◆ propfunc() [5/16]

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

◆ propfunc() [6/16]

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

◆ propfunc() [7/16]

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

◆ propfunc() [8/16]

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

◆ propfunc() [9/16]

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

◆ propfunc() [10/16]

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

◆ propfunc() [11/16]

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

◆ propfunc() [12/16]

SinglePhaseFluidProperties::propfunc ( p  ,
v  ,
 
)

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  ,
 
)

◆ propfunc() [14/16]

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

◆ propfunc() [15/16]

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

◆ propfunc() [16/16]

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

◆ propfuncWithDefault() [1/2]

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

◆ propfuncWithDefault() [2/2]

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

◆ 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
virtual

Definition at line 242 of file SinglePhaseFluidProperties.C.

250 {
251  rho_from_p_T(p, T, rho, drho_dp, drho_dT);
252  e_from_p_T(p, T, e, de_dp, de_dT);
253 }

◆ 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
virtual

Definition at line 277 of file SinglePhaseFluidProperties.C.

281 {
282  rho = rho_from_p_T(p, T);
283  mu = mu_from_p_T(p, T);
284 }

◆ 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
virtual

Reimplemented in Water97FluidProperties, CO2FluidProperties, HydrogenFluidProperties, and NitrogenFluidProperties.

Definition at line 263 of file SinglePhaseFluidProperties.C.

271 {
272  rho_from_p_T(p, T, rho, drho_dp, drho_dT);
273  mu_from_p_T(p, T, mu, dmu_dp, dmu_dT);
274 }

◆ rho_mu_from_p_T() [3/3]

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

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.

257 {
258  rho = rho_from_p_T(p, T);
259  mu = mu_from_p_T(p, T);
260 }

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.

39 {}

◆ threadJoin()

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

Definition at line 38 of file FluidProperties.h.

38 {}

◆ triplePointPressure()

Real SinglePhaseFluidProperties::triplePointPressure ( ) const
virtual

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.

133 {
134  mooseError(name(), ": ", __PRETTY_FUNCTION__, " not implemented.");
135 }

◆ triplePointTemperature()

Real SinglePhaseFluidProperties::triplePointTemperature ( ) const
virtual

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.

139 {
140  mooseError(name(), ": ", __PRETTY_FUNCTION__, " not implemented.");
141 }

◆ v_e_spndl_from_T()

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

Specific internal energy from temperature and specific volume.

Parameters
[in]Ttemperature
[in]vspecific volume

Reimplemented in IdealGasFluidProperties, and StiffenedGasFluidProperties.

Definition at line 292 of file SinglePhaseFluidProperties.C.

293 {
294  mooseError(name(), ": ", __PRETTY_FUNCTION__, " not implemented.");
295 }

Referenced by IdealRealGasMixtureFluidProperties::v_from_p_T().

◆ vaporPressure() [1/3]

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

Definition at line 198 of file SinglePhaseFluidProperties.C.

199 {
200  Real p = 0.0;
201  Real temperature = T.value();
202  Real dpdT = 0.0;
203 
204  vaporPressure(temperature, p, dpdT);
205 
206  DualReal result = p;
207  result.derivatives() = T.derivatives() * dpdT;
208 
209  return result;
210 }

◆ vaporPressure() [2/3]

Real SinglePhaseFluidProperties::vaporPressure ( Real  T) const
virtual

Vapor pressure.

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

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

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

Definition at line 177 of file SinglePhaseFluidProperties.C.

178 {
179  mooseError(name(), ": ", __PRETTY_FUNCTION__, " not implemented.");
180 }

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

◆ vaporPressure() [3/3]

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

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

Definition at line 189 of file SinglePhaseFluidProperties.C.

190 {
191  fluidPropError(name(), ": ", __PRETTY_FUNCTION__, " derivatives not implemented.");
192 
193  dp_dT = 0.0;
194  p = vaporPressure(T);
195 }

◆ vaporTemperature() [1/3]

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

Definition at line 227 of file SinglePhaseFluidProperties.C.

228 {
229  Real T = 0.0;
230  Real pressure = p.value();
231  Real dTdp = 0.0;
232 
233  vaporTemperature(pressure, T, dTdp);
234 
235  DualReal result = T;
236  result.derivatives() = p.derivatives() * dTdp;
237 
238  return result;
239 }

◆ vaporTemperature() [2/3]

Real SinglePhaseFluidProperties::vaporTemperature ( Real  p) const
virtual

Vapor temperature.

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

Parameters
pfluid pressure (Pa)
[out]saturationtemperature (K)
[out]derivativeof saturation temperature wrt pressure

Reimplemented in Water97FluidProperties.

Definition at line 212 of file SinglePhaseFluidProperties.C.

213 {
214  mooseError(name(), ": ", __PRETTY_FUNCTION__, " not implemented.");
215 }

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

◆ vaporTemperature() [3/3]

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

Reimplemented in Water97FluidProperties.

Definition at line 218 of file SinglePhaseFluidProperties.C.

219 {
220  fluidPropError(name(), ": ", __PRETTY_FUNCTION__, " derivatives not implemented.");
221 
222  dT_dp = 0.0;
223  T = vaporTemperature(p);
224 }

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 fluidPropError().

◆ _R

const Real FluidProperties::_R = 8.3144598
staticinherited

◆ _T_c2k

const Real FluidProperties::_T_c2k
protectedinherited

◆ h [1/2]

e e e e SinglePhaseFluidProperties::h

◆ h [2/2]

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

Definition at line 183 of file SinglePhaseFluidProperties.h.

◆ p [1/6]

e e e e p h SinglePhaseFluidProperties::p

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(), 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(), 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(), vaporPressure(), Water97FluidProperties::vaporTemperature(), vaporTemperature(), and TabulatedFluidProperties::writeTabulatedData().

◆ p [2/6]

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

Definition at line 171 of file SinglePhaseFluidProperties.h.

◆ p [3/6]

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

Definition at line 173 of file SinglePhaseFluidProperties.h.

◆ p [4/6]

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

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

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

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)

Definition at line 190 of file SinglePhaseFluidProperties.h.

◆ rho

e e e e p h T SinglePhaseFluidProperties::rho

◆ T [1/3]

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

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(), 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(), 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(), vaporPressure(), Water97FluidProperties::vaporTemperature(), and vaporTemperature().

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

Definition at line 179 of file SinglePhaseFluidProperties.h.

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

Definition at line 181 of file SinglePhaseFluidProperties.h.

◆ v [1/6]

SinglePhaseFluidProperties::v

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

Definition at line 157 of file SinglePhaseFluidProperties.h.

◆ v [3/6]

e e SinglePhaseFluidProperties::v

Definition at line 159 of file SinglePhaseFluidProperties.h.

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e e e SinglePhaseFluidProperties::v

Definition at line 161 of file SinglePhaseFluidProperties.h.

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e e e e p SinglePhaseFluidProperties::v

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

Definition at line 189 of file SinglePhaseFluidProperties.h.


The documentation for this class was generated from the following files:
FluidProperties::FluidProperties
FluidProperties(const InputParameters &parameters)
Definition: FluidProperties.C:27
SinglePhaseFluidProperties::T
e e e e p h T T T T T T
Definition: SinglePhaseFluidProperties.h:177
SinglePhaseFluidProperties::rho
e e e e p h T rho
Definition: SinglePhaseFluidProperties.h:169
SinglePhaseFluidProperties::vaporPressure
virtual Real vaporPressure(Real T) const
Vapor pressure.
Definition: SinglePhaseFluidProperties.C:177
SinglePhaseFluidProperties::vaporTemperature
virtual Real vaporTemperature(Real p) const
Vapor temperature.
Definition: SinglePhaseFluidProperties.C:212
name
const std::string name
Definition: Setup.h:21
SinglePhaseFluidProperties::fluidPropError
void fluidPropError(Args... args) const
Definition: SinglePhaseFluidProperties.h:326
NS::temperature
const std::string temperature
Definition: NS.h:26
FluidProperties::_allow_imperfect_jacobians
const bool _allow_imperfect_jacobians
Flag to set unimplemented Jacobian entries to zero.
Definition: FluidProperties.h:48
SinglePhaseFluidProperties::p
e e e e p h p
Definition: SinglePhaseFluidProperties.h:167
NS::pressure
const std::string pressure
Definition: NS.h:25