www.mooseframework.org
Public Types | Public Member Functions | Static Public Member Functions | Public Attributes | Static Public Attributes | Protected Member Functions | Static Protected Member Functions | Protected Attributes | Static Protected Attributes | List of all members
MethaneFluidProperties Class Reference

Methane (CH4) fluid properties as a function of pressure (Pa) and temperature (K). More...

#include <MethaneFluidProperties.h>

Inheritance diagram for MethaneFluidProperties:
[legend]

Public Types

typedef DataFileName DataFileParameterType
 

Public Member Functions

 MethaneFluidProperties (const InputParameters &parameters)
 
virtual ~MethaneFluidProperties ()
 
virtual std::string fluidName () const override
 
virtual Real molarMass () const override
 Fluid name. More...
 
virtual Real mu_from_p_T (Real pressure, Real temperature) const override
 
virtual void mu_from_p_T (Real pressure, Real temperature, Real &mu, Real &dmu_dp, Real &dmu_dT) const override
 
virtual Real k_from_p_T (Real pressure, Real temperature) const override
 
virtual void k_from_p_T (Real pressure, Real temperature, Real &k, Real &dk_dp, Real &dk_dT) const override
 
virtual std::vector< RealhenryCoefficients () const override
 Henry's law coefficients for dissolution in water. 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 vaporPressure (Real temperature) const override
 Vapor pressure. More...
 
virtual void vaporPressure (Real temperature, Real &psat, Real &dpsat_dT) const override
 
Real saturatedLiquidDensity (Real temperature) const
 Saturated liquid density of CH4 Valid for temperatures between the triple point temperature and critical temperature. More...
 
Real saturatedVaporDensity (Real temperature) const
 Saturated vapor density of CH4 Valid for temperatures between the triple point temperature and critical 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 p, Real T, Real &e, Real &de_dp, Real &de_dT) const override
 
virtual Real c_from_p_T (Real pressure, Real temperature) 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 s_from_p_T (Real pressure, Real temperature) const override
 
virtual void s_from_p_T (Real p, Real T, Real &s, Real &ds_dp, Real &ds_dT) const override
 
virtual Real h_from_p_T (Real pressure, Real temperature) const override
 
virtual void h_from_p_T (Real p, Real T, Real &h, Real &dh_dp, Real &dh_dT) const override
 
virtual Real p_from_rho_T (Real rho, Real T) const
 Pressure as a function of density and temperature. More...
 
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...
 
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
 
template<typename CppType >
void v_e_from_p_T (const CppType &p, const CppType &T, CppType &v, CppType &e) const
 
template<typename CppType >
void v_e_from_p_T (const CppType &p, const CppType &T, CppType &v, CppType &dv_dp, CppType &dv_dT, CppType &e, CppType &de_dp, CppType &de_dT) const
 
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
 
template<typename CppType >
void p_T_from_v_e (const CppType &v, const CppType &e, Real p0, Real T0, CppType &p, CppType &T, bool &conversion_succeeded) const
 Determines (p,T) from (v,e) using Newton Solve in 2D Useful for conversion between different sets of state variables. More...
 
template<typename T >
void p_T_from_v_h (const T &v, const T &h, Real p0, Real T0, T &pressure, T &temperature, bool &conversion_succeeded) const
 Determines (p,T) from (v,h) using Newton Solve in 2D Useful for conversion between different sets of state variables. More...
 
template<typename T >
void p_T_from_h_s (const T &h, const T &s, Real p0, Real T0, T &pressure, T &temperature, bool &conversion_succeeded) const
 Determines (p,T) from (h,s) using Newton Solve in 2D Useful for conversion between different sets of state variables. More...
 
template<>
std::pair< Real, RealmakeZeroAndOne (const Real &)
 
virtual void execute () final
 
virtual void initialize () final
 
virtual void finalize () final
 
virtual void threadJoin (const UserObject &) final
 
virtual void subdomainSetup () final
 
bool needThreadedCopy () const override final
 
SubProblemgetSubProblem () const
 
bool shouldDuplicateInitialExecution () const
 
virtual Real spatialValue (const Point &) const
 
virtual const std::vector< Point > spatialPoints () const
 
void gatherSum (T &value)
 
void gatherMax (T &value)
 
void gatherMin (T &value)
 
void gatherProxyValueMax (T1 &value, T2 &proxy)
 
void gatherProxyValueMin (T1 &value, T2 &proxy)
 
void setPrimaryThreadCopy (UserObject *primary)
 
UserObjectprimaryThreadCopy ()
 
std::set< UserObjectName > getDependObjects () const
 
const std::set< std::string > & getRequestedItems () override
 
const std::set< std::string > & getSuppliedItems () override
 
unsigned int systemNumber () const
 
virtual bool enabled () const
 
MooseAppgetMooseApp () const
 
const std::string & type () const
 
virtual const std::string & name () const
 
std::string typeAndName () const
 
std::string errorPrefix (const std::string &error_type) const
 
void callMooseError (std::string msg, const bool with_prefix) const
 
MooseObjectParameterName uniqueParameterName (const std::string &parameter_name) const
 
const InputParametersparameters () const
 
MooseObjectName uniqueName () const
 
const TgetParam (const std::string &name) const
 
std::vector< std::pair< T1, T2 > > getParam (const std::string &param1, const std::string &param2) const
 
const TgetRenamedParam (const std::string &old_name, const std::string &new_name) const
 
T getCheckedPointerParam (const std::string &name, const std::string &error_string="") const
 
bool isParamValid (const std::string &name) const
 
bool isParamSetByUser (const std::string &nm) const
 
void paramError (const std::string &param, Args... args) const
 
void paramWarning (const std::string &param, Args... args) const
 
void paramInfo (const std::string &param, Args... args) const
 
void connectControllableParams (const std::string &parameter, const std::string &object_type, const std::string &object_name, const std::string &object_parameter) const
 
void mooseError (Args &&... args) const
 
void mooseErrorNonPrefixed (Args &&... args) const
 
void mooseDocumentedError (const std::string &repo_name, const unsigned int issue_num, Args &&... args) const
 
void mooseWarning (Args &&... args) const
 
void mooseWarningNonPrefixed (Args &&... args) const
 
void mooseDeprecated (Args &&... args) const
 
void mooseInfo (Args &&... args) const
 
std::string getDataFileName (const std::string &param) const
 
std::string getDataFileNameByName (const std::string &name, const std::string *param=nullptr) const
 
virtual void initialSetup ()
 
virtual void timestepSetup ()
 
virtual void jacobianSetup ()
 
virtual void residualSetup ()
 
virtual void customSetup (const ExecFlagType &)
 
const ExecFlagEnumgetExecuteOnEnum () const
 
UserObjectName getUserObjectName (const std::string &param_name) const
 
const TgetUserObject (const std::string &param_name, bool is_dependency=true) const
 
const TgetUserObjectByName (const UserObjectName &object_name, bool is_dependency=true) const
 
const UserObjectgetUserObjectBase (const std::string &param_name, bool is_dependency=true) const
 
const UserObjectgetUserObjectBaseByName (const UserObjectName &object_name, bool is_dependency=true) const
 
const GenericMaterialProperty< T, is_ad > & getGenericMaterialProperty (const std::string &name, MaterialData &material_data, const unsigned int state=0)
 
const GenericMaterialProperty< T, is_ad > & getGenericMaterialProperty (const std::string &name, const unsigned int state=0)
 
const GenericMaterialProperty< T, is_ad > & getGenericMaterialProperty (const std::string &name, const unsigned int state=0)
 
const MaterialProperty< T > & getMaterialProperty (const std::string &name, MaterialData &material_data, const unsigned int state=0)
 
const MaterialProperty< T > & getMaterialProperty (const std::string &name, const unsigned int state=0)
 
const MaterialProperty< T > & getMaterialProperty (const std::string &name, const unsigned int state=0)
 
const ADMaterialProperty< T > & getADMaterialProperty (const std::string &name, MaterialData &material_data)
 
const ADMaterialProperty< T > & getADMaterialProperty (const std::string &name)
 
const ADMaterialProperty< T > & getADMaterialProperty (const std::string &name)
 
const MaterialProperty< T > & getMaterialPropertyOld (const std::string &name, MaterialData &material_data)
 
const MaterialProperty< T > & getMaterialPropertyOld (const std::string &name)
 
const MaterialProperty< T > & getMaterialPropertyOld (const std::string &name)
 
const MaterialProperty< T > & getMaterialPropertyOlder (const std::string &name, MaterialData &material_data)
 
const MaterialProperty< T > & getMaterialPropertyOlder (const std::string &name)
 
const MaterialProperty< T > & getMaterialPropertyOlder (const std::string &name)
 
const GenericMaterialProperty< T, is_ad > & getGenericMaterialPropertyByName (const MaterialPropertyName &name, MaterialData &material_data, const unsigned int state)
 
const GenericMaterialProperty< T, is_ad > & getGenericMaterialPropertyByName (const MaterialPropertyName &name, const unsigned int state=0)
 
const GenericMaterialProperty< T, is_ad > & getGenericMaterialPropertyByName (const MaterialPropertyName &name, const unsigned int state=0)
 
const MaterialProperty< T > & getMaterialPropertyByName (const MaterialPropertyName &name, MaterialData &material_data, const unsigned int state=0)
 
const MaterialProperty< T > & getMaterialPropertyByName (const MaterialPropertyName &name, const unsigned int state=0)
 
const MaterialProperty< T > & getMaterialPropertyByName (const MaterialPropertyName &name, const unsigned int state=0)
 
const ADMaterialProperty< T > & getADMaterialPropertyByName (const MaterialPropertyName &name, MaterialData &material_data)
 
const ADMaterialProperty< T > & getADMaterialPropertyByName (const MaterialPropertyName &name)
 
const ADMaterialProperty< T > & getADMaterialPropertyByName (const MaterialPropertyName &name)
 
const MaterialProperty< T > & getMaterialPropertyOldByName (const MaterialPropertyName &name, MaterialData &material_data)
 
const MaterialProperty< T > & getMaterialPropertyOldByName (const MaterialPropertyName &name)
 
const MaterialProperty< T > & getMaterialPropertyOldByName (const MaterialPropertyName &name)
 
const MaterialProperty< T > & getMaterialPropertyOlderByName (const MaterialPropertyName &name, MaterialData &material_data)
 
const MaterialProperty< T > & getMaterialPropertyOlderByName (const MaterialPropertyName &name)
 
const MaterialProperty< T > & getMaterialPropertyOlderByName (const MaterialPropertyName &name)
 
std::pair< const MaterialProperty< T > *, std::set< SubdomainID > > getBlockMaterialProperty (const MaterialPropertyName &name)
 
const GenericMaterialProperty< T, is_ad > & getGenericZeroMaterialProperty (const std::string &name)
 
const GenericMaterialProperty< T, is_ad > & getGenericZeroMaterialProperty ()
 
const GenericMaterialProperty< T, is_ad > & getGenericZeroMaterialPropertyByName (const std::string &prop_name)
 
const MaterialProperty< T > & getZeroMaterialProperty (Ts... args)
 
std::set< SubdomainIDgetMaterialPropertyBlocks (const std::string &name)
 
std::vector< SubdomainName > getMaterialPropertyBlockNames (const std::string &name)
 
std::set< BoundaryIDgetMaterialPropertyBoundaryIDs (const std::string &name)
 
std::vector< BoundaryName > getMaterialPropertyBoundaryNames (const std::string &name)
 
void checkBlockAndBoundaryCompatibility (std::shared_ptr< MaterialBase > discrete)
 
std::unordered_map< SubdomainID, std::vector< MaterialBase *> > buildRequiredMaterials (bool allow_stateful=true)
 
void statefulPropertiesAllowed (bool)
 
bool getMaterialPropertyCalled () const
 
const std::unordered_set< unsigned int > & getMatPropDependencies () const
 
virtual void resolveOptionalProperties ()
 
const GenericMaterialProperty< T, is_ad > & getPossiblyConstantGenericMaterialPropertyByName (const MaterialPropertyName &prop_name, MaterialData &material_data, const unsigned int state)
 
bool isImplicit ()
 
bool hasUserObject (const std::string &param_name) const
 
bool hasUserObject (const std::string &param_name) const
 
bool hasUserObject (const std::string &param_name) const
 
bool hasUserObject (const std::string &param_name) const
 
bool hasUserObjectByName (const UserObjectName &object_name) const
 
bool hasUserObjectByName (const UserObjectName &object_name) const
 
bool hasUserObjectByName (const UserObjectName &object_name) const
 
bool hasUserObjectByName (const UserObjectName &object_name) const
 
const GenericOptionalMaterialProperty< T, is_ad > & getGenericOptionalMaterialProperty (const std::string &name, const unsigned int state=0)
 
const GenericOptionalMaterialProperty< T, is_ad > & getGenericOptionalMaterialProperty (const std::string &name, const unsigned int state=0)
 
const OptionalMaterialProperty< T > & getOptionalMaterialProperty (const std::string &name, const unsigned int state=0)
 
const OptionalMaterialProperty< T > & getOptionalMaterialProperty (const std::string &name, const unsigned int state=0)
 
const OptionalADMaterialProperty< T > & getOptionalADMaterialProperty (const std::string &name)
 
const OptionalADMaterialProperty< T > & getOptionalADMaterialProperty (const std::string &name)
 
const OptionalMaterialProperty< T > & getOptionalMaterialPropertyOld (const std::string &name)
 
const OptionalMaterialProperty< T > & getOptionalMaterialPropertyOld (const std::string &name)
 
const OptionalMaterialProperty< T > & getOptionalMaterialPropertyOlder (const std::string &name)
 
const OptionalMaterialProperty< T > & getOptionalMaterialPropertyOlder (const std::string &name)
 
MaterialBasegetMaterial (const std::string &name)
 
MaterialBasegetMaterial (const std::string &name)
 
MaterialBasegetMaterialByName (const std::string &name, bool no_warn=false)
 
MaterialBasegetMaterialByName (const std::string &name, bool no_warn=false)
 
bool hasMaterialProperty (const std::string &name)
 
bool hasMaterialProperty (const std::string &name)
 
bool hasMaterialPropertyByName (const std::string &name)
 
bool hasMaterialPropertyByName (const std::string &name)
 
bool hasADMaterialProperty (const std::string &name)
 
bool hasADMaterialProperty (const std::string &name)
 
bool hasADMaterialPropertyByName (const std::string &name)
 
bool hasADMaterialPropertyByName (const std::string &name)
 
bool hasGenericMaterialProperty (const std::string &name)
 
bool hasGenericMaterialProperty (const std::string &name)
 
bool hasGenericMaterialPropertyByName (const std::string &name)
 
bool hasGenericMaterialPropertyByName (const std::string &name)
 
const FunctiongetFunction (const std::string &name) const
 
const FunctiongetFunctionByName (const FunctionName &name) const
 
bool hasFunction (const std::string &param_name) const
 
bool hasFunctionByName (const FunctionName &name) const
 
bool isDefaultPostprocessorValue (const std::string &param_name, const unsigned int index=0) const
 
bool hasPostprocessor (const std::string &param_name, const unsigned int index=0) const
 
bool hasPostprocessorByName (const PostprocessorName &name) const
 
std::size_t coupledPostprocessors (const std::string &param_name) const
 
const PostprocessorName & getPostprocessorName (const std::string &param_name, const unsigned int index=0) const
 
const VectorPostprocessorValuegetVectorPostprocessorValue (const std::string &param_name, const std::string &vector_name) const
 
const VectorPostprocessorValuegetVectorPostprocessorValue (const std::string &param_name, const std::string &vector_name, bool needs_broadcast) const
 
const VectorPostprocessorValuegetVectorPostprocessorValueByName (const VectorPostprocessorName &name, const std::string &vector_name) const
 
const VectorPostprocessorValuegetVectorPostprocessorValueByName (const VectorPostprocessorName &name, const std::string &vector_name, bool needs_broadcast) const
 
const VectorPostprocessorValuegetVectorPostprocessorValueOld (const std::string &param_name, const std::string &vector_name) const
 
const VectorPostprocessorValuegetVectorPostprocessorValueOld (const std::string &param_name, const std::string &vector_name, bool needs_broadcast) const
 
const VectorPostprocessorValuegetVectorPostprocessorValueOldByName (const VectorPostprocessorName &name, const std::string &vector_name) const
 
const VectorPostprocessorValuegetVectorPostprocessorValueOldByName (const VectorPostprocessorName &name, const std::string &vector_name, bool needs_broadcast) const
 
const ScatterVectorPostprocessorValuegetScatterVectorPostprocessorValue (const std::string &param_name, const std::string &vector_name) const
 
const ScatterVectorPostprocessorValuegetScatterVectorPostprocessorValueByName (const VectorPostprocessorName &name, const std::string &vector_name) const
 
const ScatterVectorPostprocessorValuegetScatterVectorPostprocessorValueOld (const std::string &param_name, const std::string &vector_name) const
 
const ScatterVectorPostprocessorValuegetScatterVectorPostprocessorValueOldByName (const VectorPostprocessorName &name, const std::string &vector_name) const
 
bool hasVectorPostprocessor (const std::string &param_name, const std::string &vector_name) const
 
bool hasVectorPostprocessor (const std::string &param_name) const
 
bool hasVectorPostprocessorByName (const VectorPostprocessorName &name, const std::string &vector_name) const
 
bool hasVectorPostprocessorByName (const VectorPostprocessorName &name) const
 
const VectorPostprocessorName & getVectorPostprocessorName (const std::string &param_name) const
 
TgetSampler (const std::string &name)
 
SamplergetSampler (const std::string &name)
 
TgetSamplerByName (const SamplerName &name)
 
SamplergetSamplerByName (const SamplerName &name)
 
virtual void meshChanged ()
 
const std::vector< MooseVariableScalar *> & getCoupledMooseScalarVars ()
 
const std::set< TagID > & getScalarVariableCoupleableVectorTags () const
 
const std::set< TagID > & getScalarVariableCoupleableMatrixTags () const
 
PerfGraphperfGraph ()
 
const PostprocessorValuegetPostprocessorValue (const std::string &param_name, const unsigned int index=0) const
 
const PostprocessorValuegetPostprocessorValue (const std::string &param_name, const unsigned int index=0) const
 
const PostprocessorValuegetPostprocessorValueOld (const std::string &param_name, const unsigned int index=0) const
 
const PostprocessorValuegetPostprocessorValueOld (const std::string &param_name, const unsigned int index=0) const
 
const PostprocessorValuegetPostprocessorValueOlder (const std::string &param_name, const unsigned int index=0) const
 
const PostprocessorValuegetPostprocessorValueOlder (const std::string &param_name, const unsigned int index=0) const
 
virtual const PostprocessorValuegetPostprocessorValueByName (const PostprocessorName &name) const
 
virtual const PostprocessorValuegetPostprocessorValueByName (const PostprocessorName &name) const
 
const PostprocessorValuegetPostprocessorValueOldByName (const PostprocessorName &name) const
 
const PostprocessorValuegetPostprocessorValueOldByName (const PostprocessorName &name) const
 
const PostprocessorValuegetPostprocessorValueOlderByName (const PostprocessorName &name) const
 
const PostprocessorValuegetPostprocessorValueOlderByName (const PostprocessorName &name) const
 
bool isVectorPostprocessorDistributed (const std::string &param_name) const
 
bool isVectorPostprocessorDistributed (const std::string &param_name) const
 
bool isVectorPostprocessorDistributedByName (const VectorPostprocessorName &name) const
 
bool isVectorPostprocessorDistributedByName (const VectorPostprocessorName &name) const
 
const DistributiongetDistribution (const std::string &name) const
 
const TgetDistribution (const std::string &name) const
 
const DistributiongetDistribution (const std::string &name) const
 
const TgetDistribution (const std::string &name) const
 
const DistributiongetDistributionByName (const DistributionName &name) const
 
const TgetDistributionByName (const std::string &name) const
 
const DistributiongetDistributionByName (const DistributionName &name) const
 
const TgetDistributionByName (const std::string &name) const
 
const Parallel::Communicator & comm () const
 
processor_id_type n_processors () const
 
processor_id_type processor_id () const
 

Static Public Member Functions

static InputParameters validParams ()
 
static void sort (typename std::vector< T > &vector)
 
static void sortDFS (typename std::vector< T > &vector)
 
static void cyclicDependencyError (CyclicDependencyException< T2 > &e, const std::string &header)
 

Public Attributes

const ConsoleStream _console
 

Static Public Attributes

static const Real _R = 8.3144598
 Universal gas constant (J/mol/K) More...
 
static constexpr PropertyValue::id_type default_property_id
 
static constexpr PropertyValue::id_type zero_property_id
 
static constexpr auto SYSTEM
 
static constexpr auto NAME
 

Protected Member Functions

virtual Real alpha (Real delta, Real tau) const override
 Helmholtz free energy. More...
 
virtual Real dalpha_ddelta (Real delta, Real tau) const override
 Derivative of Helmholtz free energy wrt delta. More...
 
virtual Real dalpha_dtau (Real delta, Real tau) const override
 Derivative of Helmholtz free energy wrt tau. More...
 
virtual Real d2alpha_ddelta2 (Real delta, Real tau) const override
 Second derivative of Helmholtz free energy wrt delta. More...
 
virtual Real d2alpha_dtau2 (Real delta, Real tau) const override
 Second derivative of Helmholtz free energy wrt tau. More...
 
virtual Real d2alpha_ddeltatau (Real delta, Real tau) const override
 Second derivative of Helmholtz free energy wrt delta and tau. More...
 
virtual void addPostprocessorDependencyHelper (const PostprocessorName &name) const override
 
virtual void addVectorPostprocessorDependencyHelper (const VectorPostprocessorName &name) const override
 
virtual void addUserObjectDependencyHelper (const UserObject &uo) const override
 
void addReporterDependencyHelper (const ReporterName &reporter_name) override
 
const ReporterNamegetReporterName (const std::string &param_name) const
 
TdeclareRestartableData (const std::string &data_name, Args &&... args)
 
ManagedValue< TdeclareManagedRestartableDataWithContext (const std::string &data_name, void *context, Args &&... args)
 
const TgetRestartableData (const std::string &data_name) const
 
TdeclareRestartableDataWithContext (const std::string &data_name, void *context, Args &&... args)
 
TdeclareRecoverableData (const std::string &data_name, Args &&... args)
 
TdeclareRestartableDataWithObjectName (const std::string &data_name, const std::string &object_name, Args &&... args)
 
TdeclareRestartableDataWithObjectNameWithContext (const std::string &data_name, const std::string &object_name, void *context, Args &&... args)
 
std::string restartableName (const std::string &data_name) const
 
const TgetMeshProperty (const std::string &data_name, const std::string &prefix)
 
const TgetMeshProperty (const std::string &data_name)
 
bool hasMeshProperty (const std::string &data_name, const std::string &prefix) const
 
bool hasMeshProperty (const std::string &data_name, const std::string &prefix) const
 
bool hasMeshProperty (const std::string &data_name) const
 
bool hasMeshProperty (const std::string &data_name) const
 
std::string meshPropertyName (const std::string &data_name) const
 
bool isCoupledScalar (const std::string &var_name, unsigned int i=0) const
 
unsigned int coupledScalarComponents (const std::string &var_name) const
 
unsigned int coupledScalar (const std::string &var_name, unsigned int comp=0) const
 
Order coupledScalarOrder (const std::string &var_name, unsigned int comp=0) const
 
const VariableValuecoupledScalarValue (const std::string &var_name, unsigned int comp=0) const
 
const ADVariableValueadCoupledScalarValue (const std::string &var_name, unsigned int comp=0) const
 
const GenericVariableValue< is_ad > & coupledGenericScalarValue (const std::string &var_name, unsigned int comp=0) const
 
const GenericVariableValue< false > & coupledGenericScalarValue (const std::string &var_name, const unsigned int comp) const
 
const GenericVariableValue< true > & coupledGenericScalarValue (const std::string &var_name, const unsigned int comp) const
 
const VariableValuecoupledVectorTagScalarValue (const std::string &var_name, TagID tag, unsigned int comp=0) const
 
const VariableValuecoupledMatrixTagScalarValue (const std::string &var_name, TagID tag, unsigned int comp=0) const
 
const VariableValuecoupledScalarValueOld (const std::string &var_name, unsigned int comp=0) const
 
const VariableValuecoupledScalarValueOlder (const std::string &var_name, unsigned int comp=0) const
 
const VariableValuecoupledScalarDot (const std::string &var_name, unsigned int comp=0) const
 
const ADVariableValueadCoupledScalarDot (const std::string &var_name, unsigned int comp=0) const
 
const VariableValuecoupledScalarDotDot (const std::string &var_name, unsigned int comp=0) const
 
const VariableValuecoupledScalarDotOld (const std::string &var_name, unsigned int comp=0) const
 
const VariableValuecoupledScalarDotDotOld (const std::string &var_name, unsigned int comp=0) const
 
const VariableValuecoupledScalarDotDu (const std::string &var_name, unsigned int comp=0) const
 
const VariableValuecoupledScalarDotDotDu (const std::string &var_name, unsigned int comp=0) const
 
const MooseVariableScalargetScalarVar (const std::string &var_name, unsigned int comp) const
 
PerfID registerTimedSection (const std::string &section_name, const unsigned int level) const
 
PerfID registerTimedSection (const std::string &section_name, const unsigned int level, const std::string &live_message, const bool print_dots=true) const
 
std::string timedSectionName (const std::string &section_name) const
 
virtual void checkMaterialProperty (const std::string &name, const unsigned int state)
 
void markMatPropRequested (const std::string &)
 
MaterialPropertyName getMaterialPropertyName (const std::string &name) const
 
void checkExecutionStage ()
 
Moose::StateArg determineState () const
 
const TgetReporterValue (const std::string &param_name, const std::size_t time_index=0)
 
const TgetReporterValue (const std::string &param_name, ReporterMode mode, const std::size_t time_index=0)
 
const TgetReporterValue (const std::string &param_name, const std::size_t time_index=0)
 
const TgetReporterValue (const std::string &param_name, ReporterMode mode, const std::size_t time_index=0)
 
const TgetReporterValueByName (const ReporterName &reporter_name, const std::size_t time_index=0)
 
const TgetReporterValueByName (const ReporterName &reporter_name, ReporterMode mode, const std::size_t time_index=0)
 
const TgetReporterValueByName (const ReporterName &reporter_name, const std::size_t time_index=0)
 
const TgetReporterValueByName (const ReporterName &reporter_name, ReporterMode mode, const std::size_t time_index=0)
 
bool hasReporterValue (const std::string &param_name) const
 
bool hasReporterValue (const std::string &param_name) const
 
bool hasReporterValue (const std::string &param_name) const
 
bool hasReporterValue (const std::string &param_name) const
 
bool hasReporterValueByName (const ReporterName &reporter_name) const
 
bool hasReporterValueByName (const ReporterName &reporter_name) const
 
bool hasReporterValueByName (const ReporterName &reporter_name) const
 
bool hasReporterValueByName (const ReporterName &reporter_name) const
 
const GenericMaterialProperty< T, is_ad > * defaultGenericMaterialProperty (const std::string &name)
 
const GenericMaterialProperty< T, is_ad > * defaultGenericMaterialProperty (const std::string &name)
 
const MaterialProperty< T > * defaultMaterialProperty (const std::string &name)
 
const MaterialProperty< T > * defaultMaterialProperty (const std::string &name)
 
const ADMaterialProperty< T > * defaultADMaterialProperty (const std::string &name)
 
const ADMaterialProperty< T > * defaultADMaterialProperty (const std::string &name)
 
void flagInvalidSolutionInternal (InvalidSolutionID _invalid_solution_id) const
 
InvalidSolutionID registerInvalidSolutionInternal (const std::string &message) const
 

Static Protected Member Functions

template<typename T , typename Functor >
static void xyDerivatives (const T x, const T &y, T &z, T &dz_dx, T &dz_dy, const Functor &z_from_x_y)
 Computes the dependent variable z and its derivatives with respect to the independent variables x and y using the simple two parameter z_from_x_y functor. More...
 
template<typename T >
static std::pair< T, TmakeZeroAndOne (const T &)
 Given a type example, this method returns zero and unity reperesentations of that type (first and second members of returned pair respectively) More...
 
static std::string meshPropertyName (const std::string &data_name, const std::string &prefix)
 

Protected Attributes

const Real _Mch4
 Methane 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 std::array< Real, 5 > _a0 {{0.008449, 4.6942, 3.4865, 1.6572, 1.4115}}
 Coefficients for ideal gas component of the Helmholtz free energy. More...
 
const std::array< Real, 5 > _b0 {{3.4004324, 10.26951575, 20.43932747, 29.93744884, 79.13351945}}
 
const std::array< Real, 13 > _N1
 Coefficients for residual component of the Helmholtz free energy. More...
 
const std::array< Real, 13 > _t1
 
const std::array< unsigned int, 13 > _d1 {{1, 1, 1, 2, 2, 2, 2, 3, 4, 4, 8, 9, 10}}
 
const std::array< Real, 23 > _N2
 
const std::array< Real, 23 > _t2
 
const std::array< unsigned int, 23 > _c2
 
const std::array< unsigned int, 23 > _d2
 
const std::array< Real, 4 > _N3
 
const std::array< Real, 4 > _t3 {{2.0, 0.0, 1.0, 2.0}}
 
const std::array< int, 4 > _d3 {{2, 0, 0, 0}}
 
const std::array< Real, 4 > _alpha3 {{20.0, 40.0, 40.0, 40.0}}
 
const std::array< Real, 4 > _beta3 {{200.0, 250.0, 250.0, 250.0}}
 
const std::array< Real, 4 > _gamma3 {{1.07, 1.11, 1.11, 1.11}}
 
const std::array< Real, 4 > _D3 {{1.0, 1.0, 1.0, 1.0}}
 
const std::array< Real, 6 > _a
 Coefficients for viscosity. More...
 
const std::array< Real, 7 > _b
 Coefficients for thermal conductivity. More...
 
const Real _tolerance
 Newton's method may be used to convert between variable sets _tolerance, _T_initial_guess, and _p_initial_guess are the parameters for these iterative solves. More...
 
const Real _T_initial_guess
 
const Real _p_initial_guess
 
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...
 
SubProblem_subproblem
 
FEProblemBase_fe_problem
 
SystemBase_sys
 
const THREAD_ID _tid
 
Assembly_assembly
 
const Moose::CoordinateSystemType_coord_sys
 
const bool _duplicate_initial_execution
 
std::set< std::string > _depend_uo
 
const bool & _enabled
 
MooseApp_app
 
const std::string _type
 
const std::string _name
 
const InputParameters_pars
 
Factory_factory
 
ActionFactory_action_factory
 
const ExecFlagEnum_execute_enum
 
const ExecFlagType_current_execute_flag
 
MooseApp_restartable_app
 
const std::string _restartable_system_name
 
const THREAD_ID _restartable_tid
 
const bool _restartable_read_only
 
FEProblemBase_mci_feproblem
 
FEProblemBase_sc_fe_problem
 
const THREAD_ID _sc_tid
 
const Real_real_zero
 
const VariableValue_scalar_zero
 
const Point & _point_zero
 
MooseApp_pg_moose_app
 
const std::string _prefix
 
const InputParameters_mi_params
 
const std::string _mi_name
 
const MooseObjectName _mi_moose_object_name
 
FEProblemBase_mi_feproblem
 
SubProblem_mi_subproblem
 
const THREAD_ID _mi_tid
 
const Moose::MaterialDataType _material_data_type
 
MaterialData_material_data
 
bool _stateful_allowed
 
bool _get_material_property_called
 
std::vector< std::unique_ptr< PropertyValue > > _default_properties
 
std::unordered_set< unsigned int_material_property_dependencies
 
const MaterialPropertyName _get_suffix
 
const bool _use_interpolated_state
 
const InputParameters_ti_params
 
FEProblemBase_ti_feproblem
 
bool _is_implicit
 
Real_t
 
int_t_step
 
Real_dt
 
Real_dt_old
 
bool _is_transient
 
const Parallel::Communicator & _communicator
 

Static Protected Attributes

static const std::string _interpolated_old
 
static const std::string _interpolated_older
 
e e e e s T T T propfuncWithDefault (cp, p, T) propfuncWithDefault(cv
 
e e e e s T T T T propfuncWithDefault (mu, p, T) propfuncWithDefault(k
 
e e e e s T T T T T rho v v T s h propfuncWithDefault (beta, p, T) propfuncWithDefault(v
 
e e e e s T T T T T rho v v T 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...
 
propfunc (c, v, e) propfunc(cp
 
e e propfunc (cv, v, e) propfunc(mu
 
e e e propfunc (k, v, e) propfuncWithDefault(s
 
e e e e propfunc (s, h, p) propfunc(rho
 
e e e e s propfunc (e, v, h) propfuncWithDefault(s
 
e e e e s T propfunc (pp_sat, p, T) propfunc(mu
 
e e e e s T T propfunc (k, rho, T) propfuncWithDefault(c
 
e e e e s T T T T T propfunc (rho, p, T) propfunc(e
 
e e e e s T T T T T rho propfunc (e, T, v) propfunc(p
 
e e e e s T T T T T rho v propfunc (h, T, v) propfunc(s
 
e e e e s T T T T T rho v v propfunc (cv, T, v) propfunc(h
 
e e e e s T T T T T rho v v T propfunc (g, v, e) propfuncWithDefault(p
 
e e e e s T T T T T rho v v Tpropfunc (T, h, p) propfuncWithDefault(T
 
 v
 
v
 
e e v
 
e e e v
 
e e e e s T T T T T rho v v T s h T v
 
e e e e p
 
e e e e s p
 
e e e e s T T p
 
e e e e s T T T p
 
e e e e s T T T T p
 
e e e e s T T T T T p
 
e e e e s T T T T T rho v v p
 
e e e e s T T T T T rho v v Tp
 
e e e e s T T T T T rho v v T s h p
 
e e e e s T rho
 
e e e e s T T T T T rho T
 
e e e e s T T T T T rho v T
 
e e e e s T T T T T rho v v T h
 
e e e e s T T T T T rho v v T s h TpropfuncWithDefault (gamma, p, T)
 

Detailed Description

Methane (CH4) fluid properties as a function of pressure (Pa) and temperature (K).

Thermodynamic properties calculated from: Setzmann and Wagner, A new equation of state and tables of thermodynamic properties for methane covering the range from the melting line to 625 K at pressures up to 100 MPa, Journal of Physical and Chemical Reference Data, 20, 1061–1155 (1991)

Viscosity and thermal conductivity calculated from Irvine Jr, T. F. and Liley, P. E. (1984) Steam and Gas Tables with Computer Equations.

Definition at line 32 of file MethaneFluidProperties.h.

Constructor & Destructor Documentation

◆ MethaneFluidProperties()

MethaneFluidProperties::MethaneFluidProperties ( const InputParameters parameters)

Definition at line 24 of file MethaneFluidProperties.C.

26  _Mch4(16.0425e-3),
27  _p_critical(4.5992e6),
28  _T_critical(190.564),
29  _rho_critical(162.66),
30  _p_triple(1.169e4),
31  _T_triple(90.6941)
32 {
33 }
const Real _T_triple
Triple point temperature (K)
const Real _p_triple
Triple point pressure (Pa)
HelmholtzFluidProperties(const InputParameters &parameters)
const Real _rho_critical
Critical density (kg/m^3)
const Real _T_critical
Critical temperature (K)
const Real _Mch4
Methane molar mass (kg/mol)
const InputParameters & parameters() const
const Real _p_critical
Critical pressure (Pa)

◆ ~MethaneFluidProperties()

MethaneFluidProperties::~MethaneFluidProperties ( )
virtual

Definition at line 35 of file MethaneFluidProperties.C.

35 {}

Member Function Documentation

◆ alpha()

Real MethaneFluidProperties::alpha ( Real  delta,
Real  tau 
) const
overrideprotectedvirtual

Helmholtz free energy.

Parameters
deltascaled density (-)
tauscaled temperature (-)
Returns
alpha Helmholtz free energy

Implements HelmholtzFluidProperties.

Definition at line 208 of file MethaneFluidProperties.C.

209 {
210  // Ideal gas component of the Helmholtz free energy
211  Real alpha0 = std::log(delta) + 9.91243972 - 6.33270087 * tau + 3.0016 * std::log(tau);
212 
213  for (std::size_t i = 0; i < _a0.size(); ++i)
214  alpha0 += _a0[i] * std::log(1.0 - std::exp(-_b0[i] * tau));
215 
216  // Residual component of the Helmholtz free energy
217  Real alphar = 0.0;
218 
219  for (std::size_t i = 0; i < _t1.size(); ++i)
220  alphar += _N1[i] * MathUtils::pow(delta, _d1[i]) * std::pow(tau, _t1[i]);
221 
222  for (std::size_t i = 0; i < _t2.size(); ++i)
223  alphar += _N2[i] * MathUtils::pow(delta, _d2[i]) * std::pow(tau, _t2[i]) *
224  std::exp(-MathUtils::pow(delta, _c2[i]));
225 
226  for (std::size_t i = 0; i < _t3.size(); ++i)
227  alphar += _N3[i] * MathUtils::pow(delta, _d3[i]) * std::pow(tau, _t3[i]) *
228  std::exp(-_alpha3[i] * Utility::pow<2>(delta - _D3[i]) -
229  _beta3[i] * Utility::pow<2>(tau - _gamma3[i]));
230 
231  // The Helmholtz free energy is the sum of these two
232  return alpha0 + alphar;
233 }
const std::array< Real, 4 > _t3
const std::array< Real, 5 > _a0
Coefficients for ideal gas component of the Helmholtz free energy.
const std::array< Real, 5 > _b0
const std::array< Real, 4 > _D3
const std::array< unsigned int, 23 > _d2
const std::array< Real, 4 > _beta3
int delta(unsigned int i, unsigned int j)
Delta function, which returns zero if $i j$ and unity if $i=j$.
const std::array< Real, 13 > _t1
const std::array< Real, 4 > _N3
const std::array< Real, 13 > _N1
Coefficients for residual component of the Helmholtz free energy.
const std::array< Real, 4 > _gamma3
const std::array< unsigned int, 23 > _c2
const std::array< Real, 23 > _t2
const std::array< int, 4 > _d3
const std::array< Real, 4 > _alpha3
DIE A HORRIBLE DEATH HERE typedef LIBMESH_DEFAULT_SCALAR_TYPE Real
const std::array< unsigned int, 13 > _d1
const std::array< Real, 23 > _N2
T pow(T x, int e)
MooseUnits pow(const MooseUnits &, int)

◆ c_from_p_T()

Real HelmholtzFluidProperties::c_from_p_T ( Real  pressure,
Real  temperature 
) const
overridevirtualinherited

Definition at line 98 of file HelmholtzFluidProperties.C.

99 {
100  // Require density first
102  // Scale the input density and temperature
103  const Real delta = density / criticalDensity();
104  const Real tau = criticalTemperature() / temperature;
105 
106  const Real da_dd = dalpha_ddelta(delta, tau);
107 
108  Real w = 2.0 * delta * da_dd + delta * delta * d2alpha_ddelta2(delta, tau);
109  w -= Utility::pow<2>(delta * da_dd - delta * tau * d2alpha_ddeltatau(delta, tau)) /
110  (tau * tau * d2alpha_dtau2(delta, tau));
111 
112  return std::sqrt(_R * temperature * w / molarMass());
113 }
virtual Real d2alpha_ddeltatau(Real delta, Real tau) const =0
Second derivative of Helmholtz free energy wrt delta and tau.
virtual Real d2alpha_dtau2(Real delta, Real tau) const =0
Second derivative of Helmholtz free energy wrt tau.
virtual virtual std Real molarMass() const
Fluid name.
static const std::string density
Definition: NS.h:33
int delta(unsigned int i, unsigned int j)
Delta function, which returns zero if $i j$ and unity if $i=j$.
static const Real _R
Universal gas constant (J/mol/K)
static const std::string temperature
Definition: NS.h:57
virtual Real d2alpha_ddelta2(Real delta, Real tau) const =0
Second derivative of Helmholtz free energy wrt delta.
ADRealEigenVector< T, D, asd > sqrt(const ADRealEigenVector< T, D, asd > &)
virtual Real criticalTemperature() const
Critical temperature.
virtual Real dalpha_ddelta(Real delta, Real tau) const =0
Derivative of Helmholtz free energy wrt delta.
virtual Real rho_from_p_T(Real pressure, Real temperature) const override
virtual Real criticalDensity() const
Critical density.
DIE A HORRIBLE DEATH HERE typedef LIBMESH_DEFAULT_SCALAR_TYPE Real
static const std::string pressure
Definition: NS.h:56

◆ cp_from_p_T()

Real HelmholtzFluidProperties::cp_from_p_T ( Real  pressure,
Real  temperature 
) const
overridevirtualinherited

Definition at line 116 of file HelmholtzFluidProperties.C.

117 {
118  // Require density first
120  // Scale the input density and temperature
121  const Real delta = density / criticalDensity();
122  const Real tau = criticalTemperature() / temperature;
123 
124  const Real da_dd = dalpha_ddelta(delta, tau);
125 
126  const Real cp = _R *
127  (-tau * tau * d2alpha_dtau2(delta, tau) +
128  Utility::pow<2>(delta * da_dd - delta * tau * d2alpha_ddeltatau(delta, tau)) /
129  (2.0 * delta * da_dd + delta * delta * d2alpha_ddelta2(delta, tau))) /
130  molarMass();
131 
132  return cp;
133 }
virtual Real d2alpha_ddeltatau(Real delta, Real tau) const =0
Second derivative of Helmholtz free energy wrt delta and tau.
virtual Real d2alpha_dtau2(Real delta, Real tau) const =0
Second derivative of Helmholtz free energy wrt tau.
virtual virtual std Real molarMass() const
Fluid name.
static const std::string density
Definition: NS.h:33
int delta(unsigned int i, unsigned int j)
Delta function, which returns zero if $i j$ and unity if $i=j$.
static const Real _R
Universal gas constant (J/mol/K)
static const std::string temperature
Definition: NS.h:57
virtual Real d2alpha_ddelta2(Real delta, Real tau) const =0
Second derivative of Helmholtz free energy wrt delta.
static const std::string cp
Definition: NS.h:120
virtual Real criticalTemperature() const
Critical temperature.
virtual Real dalpha_ddelta(Real delta, Real tau) const =0
Derivative of Helmholtz free energy wrt delta.
virtual Real rho_from_p_T(Real pressure, Real temperature) const override
virtual Real criticalDensity() const
Critical density.
DIE A HORRIBLE DEATH HERE typedef LIBMESH_DEFAULT_SCALAR_TYPE Real
static const std::string pressure
Definition: NS.h:56

◆ criticalDensity()

Real MethaneFluidProperties::criticalDensity ( ) const
overridevirtual

Critical density.

Returns
critical density (kg/m^3)

Reimplemented from SinglePhaseFluidProperties.

Definition at line 62 of file MethaneFluidProperties.C.

63 {
64  return _rho_critical;
65 }
const Real _rho_critical
Critical density (kg/m^3)

◆ criticalInternalEnergy()

Real SinglePhaseFluidProperties::criticalInternalEnergy ( ) const
virtualinherited

Critical specific internal energy.

Returns
specific internal energy (J/kg)

Reimplemented in IdealGasFluidProperties, CaloricallyImperfectGas, and StiffenedGasFluidProperties.

Definition at line 297 of file SinglePhaseFluidProperties.C.

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

298 {
299  mooseError(__PRETTY_FUNCTION__, " not implemented.");
300 }
void mooseError(Args &&... args) const

◆ criticalPressure()

Real MethaneFluidProperties::criticalPressure ( ) const
overridevirtual

Critical pressure.

Returns
critical pressure (Pa)

Reimplemented from SinglePhaseFluidProperties.

Definition at line 50 of file MethaneFluidProperties.C.

51 {
52  return _p_critical;
53 }
const Real _p_critical
Critical pressure (Pa)

◆ criticalTemperature()

Real MethaneFluidProperties::criticalTemperature ( ) const
overridevirtual

Critical temperature.

Returns
critical temperature (K)

Reimplemented from SinglePhaseFluidProperties.

Definition at line 56 of file MethaneFluidProperties.C.

57 {
58  return _T_critical;
59 }
const Real _T_critical
Critical temperature (K)

◆ cv_from_p_T()

Real HelmholtzFluidProperties::cv_from_p_T ( Real  pressure,
Real  temperature 
) const
overridevirtualinherited

Definition at line 136 of file HelmholtzFluidProperties.C.

137 {
138  // Require density first
140  // Scale the input density and temperature
141  const Real delta = density / criticalDensity();
142  const Real tau = criticalTemperature() / temperature;
143 
144  return -_R * tau * tau * d2alpha_dtau2(delta, tau) / molarMass();
145 }
virtual Real d2alpha_dtau2(Real delta, Real tau) const =0
Second derivative of Helmholtz free energy wrt tau.
virtual virtual std Real molarMass() const
Fluid name.
static const std::string density
Definition: NS.h:33
int delta(unsigned int i, unsigned int j)
Delta function, which returns zero if $i j$ and unity if $i=j$.
static const Real _R
Universal gas constant (J/mol/K)
static const std::string temperature
Definition: NS.h:57
virtual Real criticalTemperature() const
Critical temperature.
virtual Real rho_from_p_T(Real pressure, Real temperature) const override
virtual Real criticalDensity() const
Critical density.
DIE A HORRIBLE DEATH HERE typedef LIBMESH_DEFAULT_SCALAR_TYPE Real
static const std::string pressure
Definition: NS.h:56

◆ d2alpha_ddelta2()

Real MethaneFluidProperties::d2alpha_ddelta2 ( Real  delta,
Real  tau 
) const
overrideprotectedvirtual

Second derivative of Helmholtz free energy wrt delta.

Parameters
deltascaled density (-)
tauscaled temperature (-)
Returns
second derivative of Helmholtz free energy wrt delta

Implements HelmholtzFluidProperties.

Definition at line 292 of file MethaneFluidProperties.C.

293 {
294  // Ideal gas component of the Helmholtz free energy
295  Real dalpha0 = -1.0 / delta / delta;
296 
297  // Residual component of the Helmholtz free energy
298  Real dalphar = 0.0;
299 
300  for (std::size_t i = 0; i < _t1.size(); ++i)
301  dalphar +=
302  _N1[i] * _d1[i] * (_d1[i] - 1.0) * MathUtils::pow(delta, _d1[i]) * std::pow(tau, _t1[i]);
303 
304  for (std::size_t i = 0; i < _t2.size(); ++i)
305  dalphar += _N2[i] * MathUtils::pow(delta, _d2[i]) * std::pow(tau, _t2[i]) *
306  std::exp(-MathUtils::pow(delta, _c2[i])) *
307  ((_d2[i] - _c2[i] * MathUtils::pow(delta, _c2[i])) *
308  (_d2[i] - 1.0 - _c2[i] * MathUtils::pow(delta, _c2[i])) -
309  _c2[i] * _c2[i] * MathUtils::pow(delta, _c2[i]));
310 
311  for (std::size_t i = 0; i < _t3.size(); ++i)
312  dalphar += _N3[i] * std::pow(tau, _t3[i]) *
313  std::exp(-_alpha3[i] * Utility::pow<2>(delta - _D3[i]) -
314  _beta3[i] * Utility::pow<2>(tau - _gamma3[i])) *
315  (-2.0 * _alpha3[i] * MathUtils::pow(delta, _d3[i] + 2) +
316  4.0 * _alpha3[i] * _alpha3[i] * MathUtils::pow(delta, _d3[i] + 2) *
317  MathUtils::pow(delta - _D3[i], 2) -
318  4.0 * _d3[i] * _alpha3[i] * MathUtils::pow(delta, _d3[i] + 1) * (delta - _D3[i]) +
319  _d3[i] * (_d3[i] - 1) * MathUtils::pow(delta, _d3[i]));
320 
321  // The Helmholtz free energy is the sum of these two
322  return dalpha0 + dalphar / delta / delta;
323 }
const std::array< Real, 4 > _t3
const std::array< Real, 4 > _D3
const std::array< unsigned int, 23 > _d2
const std::array< Real, 4 > _beta3
int delta(unsigned int i, unsigned int j)
Delta function, which returns zero if $i j$ and unity if $i=j$.
const std::array< Real, 13 > _t1
const std::array< Real, 4 > _N3
const std::array< Real, 13 > _N1
Coefficients for residual component of the Helmholtz free energy.
const std::array< Real, 4 > _gamma3
const std::array< unsigned int, 23 > _c2
const std::array< Real, 23 > _t2
const std::array< int, 4 > _d3
const std::array< Real, 4 > _alpha3
DIE A HORRIBLE DEATH HERE typedef LIBMESH_DEFAULT_SCALAR_TYPE Real
const std::array< unsigned int, 13 > _d1
const std::array< Real, 23 > _N2
T pow(T x, int e)
MooseUnits pow(const MooseUnits &, int)

◆ d2alpha_ddeltatau()

Real MethaneFluidProperties::d2alpha_ddeltatau ( Real  delta,
Real  tau 
) const
overrideprotectedvirtual

Second derivative of Helmholtz free energy wrt delta and tau.

Parameters
deltascaled density (-)
tauscaled temperature (-)
Returns
second derivative of Helmholtz free energy wrt delta and tau

Implements HelmholtzFluidProperties.

Definition at line 360 of file MethaneFluidProperties.C.

361 {
362  // Residual component of the Helmholtz free energy
363  Real dalphar = 0.0;
364 
365  for (std::size_t i = 0; i < _t1.size(); ++i)
366  dalphar += _N1[i] * _d1[i] * _t1[i] * std::pow(delta, _d1[i]) * std::pow(tau, _t1[i]);
367 
368  for (std::size_t i = 0; i < _t2.size(); ++i)
369  dalphar += _N2[i] * _t2[i] * std::pow(delta, _d2[i]) * std::pow(tau, _t2[i]) *
370  std::exp(-MathUtils::pow(delta, _c2[i])) *
371  (_d2[i] - _c2[i] * MathUtils::pow(delta, _c2[i]));
372 
373  for (std::size_t i = 0; i < _t3.size(); ++i)
374  dalphar += _N3[i] * std::pow(delta, _d3[i]) * std::pow(tau, _t3[i]) *
375  std::exp(-_alpha3[i] * Utility::pow<2>(delta - _D3[i]) -
376  _beta3[i] * Utility::pow<2>(tau - _gamma3[i])) *
377  (_d3[i] - 2.0 * _alpha3[i] * delta * (delta - _D3[i]) *
378  (_t3[i] - 2.0 * _beta3[i] * tau * (tau - _gamma3[i])));
379 
380  // The Helmholtz free energy is the sum of these two
381  return dalphar / delta / tau;
382 }
const std::array< Real, 4 > _t3
const std::array< Real, 4 > _D3
const std::array< unsigned int, 23 > _d2
const std::array< Real, 4 > _beta3
int delta(unsigned int i, unsigned int j)
Delta function, which returns zero if $i j$ and unity if $i=j$.
const std::array< Real, 13 > _t1
const std::array< Real, 4 > _N3
const std::array< Real, 13 > _N1
Coefficients for residual component of the Helmholtz free energy.
const std::array< Real, 4 > _gamma3
const std::array< unsigned int, 23 > _c2
const std::array< Real, 23 > _t2
const std::array< int, 4 > _d3
const std::array< Real, 4 > _alpha3
DIE A HORRIBLE DEATH HERE typedef LIBMESH_DEFAULT_SCALAR_TYPE Real
const std::array< unsigned int, 13 > _d1
const std::array< Real, 23 > _N2
T pow(T x, int e)
MooseUnits pow(const MooseUnits &, int)

◆ d2alpha_dtau2()

Real MethaneFluidProperties::d2alpha_dtau2 ( Real  delta,
Real  tau 
) const
overrideprotectedvirtual

Second derivative of Helmholtz free energy wrt tau.

Parameters
deltascaled density (-)
tauscaled temperature (-)
Returns
second derivative of Helmholtz free energy wrt tau

Implements HelmholtzFluidProperties.

Definition at line 326 of file MethaneFluidProperties.C.

327 {
328  // Ideal gas component of the Helmholtz free energy
329  Real dalpha0 = -3.0016 / tau / tau;
330 
331  for (std::size_t i = 0; i < _a0.size(); ++i)
332  {
333  Real exptau = std::exp(-_b0[i] * tau);
334  dalpha0 -= _a0[i] * (_b0[i] * _b0[i] * exptau / (1.0 - exptau) / (1.0 - exptau));
335  }
336 
337  // Residual component of the Helmholtz free energy
338  Real dalphar = 0.0;
339 
340  for (std::size_t i = 0; i < _t1.size(); ++i)
341  dalphar +=
342  _N1[i] * _t1[i] * (_t1[i] - 1.0) * MathUtils::pow(delta, _d1[i]) * std::pow(tau, _t1[i]);
343 
344  for (std::size_t i = 0; i < _t2.size(); ++i)
345  dalphar += _N2[i] * _t2[i] * (_t2[i] - 1.0) * MathUtils::pow(delta, _d2[i]) *
346  std::pow(tau, _t2[i]) * std::exp(-MathUtils::pow(delta, _c2[i]));
347 
348  for (std::size_t i = 0; i < _t3.size(); ++i)
349  dalphar += _N3[i] * MathUtils::pow(delta, _d3[i]) * std::pow(tau, _t3[i]) *
350  std::exp(-_alpha3[i] * Utility::pow<2>(delta - _D3[i]) -
351  _beta3[i] * Utility::pow<2>(tau - _gamma3[i])) *
352  (tau * _t3[i] - _beta3[i] * tau * tau * MathUtils::pow(tau - _gamma3[i], 2) -
353  _t3[i] - 2.0 * tau * tau * _beta3[i]);
354 
355  // The Helmholtz free energy is the sum of these two
356  return dalpha0 + dalphar / tau / tau;
357 }
const std::array< Real, 4 > _t3
const std::array< Real, 5 > _a0
Coefficients for ideal gas component of the Helmholtz free energy.
const std::array< Real, 5 > _b0
const std::array< Real, 4 > _D3
const std::array< unsigned int, 23 > _d2
const std::array< Real, 4 > _beta3
int delta(unsigned int i, unsigned int j)
Delta function, which returns zero if $i j$ and unity if $i=j$.
const std::array< Real, 13 > _t1
const std::array< Real, 4 > _N3
const std::array< Real, 13 > _N1
Coefficients for residual component of the Helmholtz free energy.
const std::array< Real, 4 > _gamma3
const std::array< unsigned int, 23 > _c2
const std::array< Real, 23 > _t2
const std::array< int, 4 > _d3
const std::array< Real, 4 > _alpha3
DIE A HORRIBLE DEATH HERE typedef LIBMESH_DEFAULT_SCALAR_TYPE Real
const std::array< unsigned int, 13 > _d1
const std::array< Real, 23 > _N2
T pow(T x, int e)
MooseUnits pow(const MooseUnits &, int)

◆ dalpha_ddelta()

Real MethaneFluidProperties::dalpha_ddelta ( Real  delta,
Real  tau 
) const
overrideprotectedvirtual

Derivative of Helmholtz free energy wrt delta.

Parameters
deltascaled density (-)
tauscaled temperature (-)
Returns
derivative of Helmholtz free energy wrt delta

Implements HelmholtzFluidProperties.

Definition at line 236 of file MethaneFluidProperties.C.

237 {
238  // Ideal gas component of the Helmholtz free energy
239  Real dalpha0 = 1.0 / delta;
240 
241  // Residual component of the Helmholtz free energy
242  Real dalphar = 0.0;
243 
244  for (std::size_t i = 0; i < _t1.size(); ++i)
245  dalphar += _N1[i] * _d1[i] * MathUtils::pow(delta, _d1[i]) * std::pow(tau, _t1[i]);
246 
247  for (std::size_t i = 0; i < _t2.size(); ++i)
248  dalphar += _N2[i] * MathUtils::pow(delta, _d2[i]) * std::pow(tau, _t2[i]) *
249  std::exp(-MathUtils::pow(delta, _c2[i])) *
250  (_d2[i] - _c2[i] * MathUtils::pow(delta, _c2[i]));
251 
252  for (std::size_t i = 0; i < _t3.size(); ++i)
253  dalphar += _N3[i] * MathUtils::pow(delta, _d3[i]) * std::pow(tau, _t3[i]) *
254  std::exp(-_alpha3[i] * Utility::pow<2>(delta - _D3[i]) -
255  _beta3[i] * Utility::pow<2>(tau - _gamma3[i])) *
256  (_d3[i] - delta * (2.0 * _alpha3[i] * (delta - _D3[i])));
257 
258  // The Helmholtz free energy is the sum of these two
259  return dalpha0 + dalphar / delta;
260 }
const std::array< Real, 4 > _t3
const std::array< Real, 4 > _D3
const std::array< unsigned int, 23 > _d2
const std::array< Real, 4 > _beta3
int delta(unsigned int i, unsigned int j)
Delta function, which returns zero if $i j$ and unity if $i=j$.
const std::array< Real, 13 > _t1
const std::array< Real, 4 > _N3
const std::array< Real, 13 > _N1
Coefficients for residual component of the Helmholtz free energy.
const std::array< Real, 4 > _gamma3
const std::array< unsigned int, 23 > _c2
const std::array< Real, 23 > _t2
const std::array< int, 4 > _d3
const std::array< Real, 4 > _alpha3
DIE A HORRIBLE DEATH HERE typedef LIBMESH_DEFAULT_SCALAR_TYPE Real
const std::array< unsigned int, 13 > _d1
const std::array< Real, 23 > _N2
T pow(T x, int e)
MooseUnits pow(const MooseUnits &, int)

◆ dalpha_dtau()

Real MethaneFluidProperties::dalpha_dtau ( Real  delta,
Real  tau 
) const
overrideprotectedvirtual

Derivative of Helmholtz free energy wrt tau.

Parameters
deltascaled density (-)
tauscaled temperature (-)
Returns
derivative of Helmholtz free energy wrt tau

Implements HelmholtzFluidProperties.

Definition at line 263 of file MethaneFluidProperties.C.

264 {
265  // Ideal gas component of the Helmholtz free energy
266  Real dalpha0 = -6.33270087 + 3.0016 / tau;
267 
268  for (std::size_t i = 0; i < _a0.size(); ++i)
269  dalpha0 += _a0[i] * _b0[i] * (1.0 / (1.0 - std::exp(-_b0[i] * tau)) - 1.0);
270 
271  // Residual component of the Helmholtz free energy
272  Real dalphar = 0.0;
273 
274  for (std::size_t i = 0; i < _t1.size(); ++i)
275  dalphar += _N1[i] * _t1[i] * MathUtils::pow(delta, _d1[i]) * std::pow(tau, _t1[i]);
276 
277  for (std::size_t i = 0; i < _t2.size(); ++i)
278  dalphar += _N2[i] * _t2[i] * MathUtils::pow(delta, _d2[i]) * std::pow(tau, _t2[i]) *
279  std::exp(-MathUtils::pow(delta, _c2[i]));
280 
281  for (std::size_t i = 0; i < _t3.size(); ++i)
282  dalphar += _N3[i] * MathUtils::pow(delta, _d3[i]) * std::pow(tau, _t3[i]) *
283  std::exp(-_alpha3[i] * Utility::pow<2>(delta - _D3[i]) -
284  _beta3[i] * Utility::pow<2>(tau - _gamma3[i])) *
285  (_t3[i] + tau * (2.0 * _beta3[i] * (tau - _gamma3[i])));
286 
287  // The Helmholtz free energy is the sum of these two
288  return dalpha0 + dalphar / tau;
289 }
const std::array< Real, 4 > _t3
const std::array< Real, 5 > _a0
Coefficients for ideal gas component of the Helmholtz free energy.
const std::array< Real, 5 > _b0
const std::array< Real, 4 > _D3
const std::array< unsigned int, 23 > _d2
const std::array< Real, 4 > _beta3
int delta(unsigned int i, unsigned int j)
Delta function, which returns zero if $i j$ and unity if $i=j$.
const std::array< Real, 13 > _t1
const std::array< Real, 4 > _N3
const std::array< Real, 13 > _N1
Coefficients for residual component of the Helmholtz free energy.
const std::array< Real, 4 > _gamma3
const std::array< unsigned int, 23 > _c2
const std::array< Real, 23 > _t2
const std::array< int, 4 > _d3
const std::array< Real, 4 > _alpha3
DIE A HORRIBLE DEATH HERE typedef LIBMESH_DEFAULT_SCALAR_TYPE Real
const std::array< unsigned int, 13 > _d1
const std::array< Real, 23 > _N2
T pow(T x, int e)
MooseUnits pow(const MooseUnits &, int)

◆ e_from_p_T() [1/2]

Real HelmholtzFluidProperties::e_from_p_T ( Real  pressure,
Real  temperature 
) const
overridevirtualinherited

Definition at line 63 of file HelmholtzFluidProperties.C.

Referenced by HelmholtzFluidProperties::e_from_p_T().

64 {
65  // Require density first
67  // Scale the input density and temperature
68  const Real delta = density / criticalDensity();
69  const Real tau = criticalTemperature() / temperature;
70 
71  return _R * temperature * tau * dalpha_dtau(delta, tau) / molarMass();
72 }
virtual virtual std Real molarMass() const
Fluid name.
static const std::string density
Definition: NS.h:33
int delta(unsigned int i, unsigned int j)
Delta function, which returns zero if $i j$ and unity if $i=j$.
static const Real _R
Universal gas constant (J/mol/K)
static const std::string temperature
Definition: NS.h:57
virtual Real criticalTemperature() const
Critical temperature.
virtual Real rho_from_p_T(Real pressure, Real temperature) const override
virtual Real dalpha_dtau(Real delta, Real tau) const =0
Derivative of Helmholtz free energy wrt tau.
virtual Real criticalDensity() const
Critical density.
DIE A HORRIBLE DEATH HERE typedef LIBMESH_DEFAULT_SCALAR_TYPE Real
static const std::string pressure
Definition: NS.h:56

◆ e_from_p_T() [2/2]

void HelmholtzFluidProperties::e_from_p_T ( Real  p,
Real  T,
Real e,
Real de_dp,
Real de_dT 
) const
overridevirtualinherited

Definition at line 75 of file HelmholtzFluidProperties.C.

77 {
78  e = this->e_from_p_T(pressure, temperature);
79 
80  // Require density first
82  // Scale the input density and temperature
83  const Real delta = density / criticalDensity();
84  const Real tau = criticalTemperature() / temperature;
85 
86  const Real da_dd = dalpha_ddelta(delta, tau);
87  const Real d2a_dd2 = d2alpha_ddelta2(delta, tau);
88  const Real d2a_ddt = d2alpha_ddeltatau(delta, tau);
89 
90  de_dp = tau * d2a_ddt / (density * (2.0 * da_dd + delta * d2a_dd2));
91  de_dT = -_R *
92  (delta * tau * d2a_ddt * (da_dd - tau * d2a_ddt) / (2.0 * da_dd + delta * d2a_dd2) +
93  tau * tau * d2alpha_dtau2(delta, tau)) /
94  molarMass();
95 }
virtual Real d2alpha_ddeltatau(Real delta, Real tau) const =0
Second derivative of Helmholtz free energy wrt delta and tau.
virtual Real d2alpha_dtau2(Real delta, Real tau) const =0
Second derivative of Helmholtz free energy wrt tau.
virtual virtual std Real molarMass() const
Fluid name.
static const std::string density
Definition: NS.h:33
int delta(unsigned int i, unsigned int j)
Delta function, which returns zero if $i j$ and unity if $i=j$.
static const Real _R
Universal gas constant (J/mol/K)
static const std::string temperature
Definition: NS.h:57
virtual Real d2alpha_ddelta2(Real delta, Real tau) const =0
Second derivative of Helmholtz free energy wrt delta.
virtual Real criticalTemperature() const
Critical temperature.
virtual Real dalpha_ddelta(Real delta, Real tau) const =0
Derivative of Helmholtz free energy wrt delta.
virtual Real rho_from_p_T(Real pressure, Real temperature) const override
virtual Real criticalDensity() const
Critical density.
DIE A HORRIBLE DEATH HERE typedef LIBMESH_DEFAULT_SCALAR_TYPE Real
static const std::string pressure
Definition: NS.h:56
virtual Real e_from_p_T(Real pressure, Real temperature) const override

◆ e_spndl_from_v()

Real SinglePhaseFluidProperties::e_spndl_from_v ( Real  v) const
virtualinherited

Specific internal energy from temperature and specific volume.

Parameters
[in]Ttemperature
[in]vspecific volume

Reimplemented in IdealGasFluidProperties, CaloricallyImperfectGas, and StiffenedGasFluidProperties.

Definition at line 457 of file SinglePhaseFluidProperties.C.

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

458 {
459  mooseError(__PRETTY_FUNCTION__, " not implemented.");
460 }
void mooseError(Args &&... args) const

◆ execute()

virtual void FluidProperties::execute ( )
inlinefinalvirtualinherited

Implements ThreadedGeneralUserObject.

Definition at line 33 of file FluidProperties.h.

33 {}

◆ finalize()

virtual void FluidProperties::finalize ( )
inlinefinalvirtualinherited

Implements ThreadedGeneralUserObject.

Definition at line 35 of file FluidProperties.h.

35 {}

◆ fluidName()

std::string MethaneFluidProperties::fluidName ( ) const
overridevirtual

Definition at line 38 of file MethaneFluidProperties.C.

39 {
40  return "methane";
41 }

◆ h_from_p_T() [1/2]

Real HelmholtzFluidProperties::h_from_p_T ( Real  pressure,
Real  temperature 
) const
overridevirtualinherited

Definition at line 183 of file HelmholtzFluidProperties.C.

Referenced by HelmholtzFluidProperties::h_from_p_T().

184 {
185  // Require density first
187  // Scale the input density and temperature
188  const Real delta = density / criticalDensity();
189  const Real tau = criticalTemperature() / temperature;
190 
191  return _R * temperature * (tau * dalpha_dtau(delta, tau) + delta * dalpha_ddelta(delta, tau)) /
192  molarMass();
193 }
virtual virtual std Real molarMass() const
Fluid name.
static const std::string density
Definition: NS.h:33
int delta(unsigned int i, unsigned int j)
Delta function, which returns zero if $i j$ and unity if $i=j$.
static const Real _R
Universal gas constant (J/mol/K)
static const std::string temperature
Definition: NS.h:57
virtual Real criticalTemperature() const
Critical temperature.
virtual Real dalpha_ddelta(Real delta, Real tau) const =0
Derivative of Helmholtz free energy wrt delta.
virtual Real rho_from_p_T(Real pressure, Real temperature) const override
virtual Real dalpha_dtau(Real delta, Real tau) const =0
Derivative of Helmholtz free energy wrt tau.
virtual Real criticalDensity() const
Critical density.
DIE A HORRIBLE DEATH HERE typedef LIBMESH_DEFAULT_SCALAR_TYPE Real
static const std::string pressure
Definition: NS.h:56

◆ h_from_p_T() [2/2]

void HelmholtzFluidProperties::h_from_p_T ( Real  p,
Real  T,
Real h,
Real dh_dp,
Real dh_dT 
) const
overridevirtualinherited

Definition at line 196 of file HelmholtzFluidProperties.C.

198 {
199  h = this->h_from_p_T(pressure, temperature);
200 
201  // Require density first
203  // Scale the input density and temperature
204  const Real delta = density / criticalDensity();
205  const Real tau = criticalTemperature() / temperature;
206 
207  const Real da_dd = dalpha_ddelta(delta, tau);
208  const Real d2a_dd2 = d2alpha_ddelta2(delta, tau);
209  const Real d2a_ddt = d2alpha_ddeltatau(delta, tau);
210 
211  dh_dp = (da_dd + delta * d2a_dd2 + tau * d2a_ddt) / (density * (2.0 * da_dd + delta * d2a_dd2));
212  dh_dT = _R *
213  (delta * da_dd * (1.0 - tau * d2a_ddt / da_dd) * (1.0 - tau * d2a_ddt / da_dd) /
214  (2.0 + delta * d2a_dd2 / da_dd) -
215  tau * tau * d2alpha_dtau2(delta, tau)) /
216  molarMass();
217 }
virtual Real d2alpha_ddeltatau(Real delta, Real tau) const =0
Second derivative of Helmholtz free energy wrt delta and tau.
virtual Real d2alpha_dtau2(Real delta, Real tau) const =0
Second derivative of Helmholtz free energy wrt tau.
virtual virtual std Real molarMass() const
Fluid name.
static const std::string density
Definition: NS.h:33
int delta(unsigned int i, unsigned int j)
Delta function, which returns zero if $i j$ and unity if $i=j$.
static const Real _R
Universal gas constant (J/mol/K)
static const std::string temperature
Definition: NS.h:57
virtual Real d2alpha_ddelta2(Real delta, Real tau) const =0
Second derivative of Helmholtz free energy wrt delta.
virtual Real criticalTemperature() const
Critical temperature.
virtual Real dalpha_ddelta(Real delta, Real tau) const =0
Derivative of Helmholtz free energy wrt delta.
virtual Real h_from_p_T(Real pressure, Real temperature) const override
virtual Real rho_from_p_T(Real pressure, Real temperature) const override
e e e e s T T T T T rho v v T h
virtual Real criticalDensity() const
Critical density.
DIE A HORRIBLE DEATH HERE typedef LIBMESH_DEFAULT_SCALAR_TYPE Real
static const std::string pressure
Definition: NS.h:56

◆ henryCoefficients()

std::vector< Real > MethaneFluidProperties::henryCoefficients ( ) const
overridevirtual

Henry's law coefficients for dissolution in water.

Returns
Henry's constant coefficients

Reimplemented from SinglePhaseFluidProperties.

Definition at line 168 of file MethaneFluidProperties.C.

169 {
170  return {-10.44708, 4.66491, 12.12986};
171 }

◆ initialize()

virtual void FluidProperties::initialize ( )
inlinefinalvirtualinherited

Implements ThreadedGeneralUserObject.

Definition at line 34 of file FluidProperties.h.

34 {}

◆ k_from_p_T() [1/2]

Real MethaneFluidProperties::k_from_p_T ( Real  pressure,
Real  temperature 
) const
overridevirtual

Definition at line 109 of file MethaneFluidProperties.C.

110 {
111  // Check the temperature is in the range of validity (200 K <= T <= 1000 K)
112  if (temperature <= 200.0 || temperature >= 1000.0)
113  mooseException(
114  "Temperature ", temperature, "K out of range (200K, 1000K) in ", name(), ": k()");
115 
116  Real kt = 0.0;
117  for (std::size_t i = 0; i < _b.size(); ++i)
118  kt += _b[i] * MathUtils::pow(temperature, i);
119 
120  return kt;
121 }
static const std::string temperature
Definition: NS.h:57
virtual const std::string & name() const
const std::array< Real, 7 > _b
Coefficients for thermal conductivity.
DIE A HORRIBLE DEATH HERE typedef LIBMESH_DEFAULT_SCALAR_TYPE Real
T pow(T x, int e)

◆ k_from_p_T() [2/2]

void MethaneFluidProperties::k_from_p_T ( Real  pressure,
Real  temperature,
Real k,
Real dk_dp,
Real dk_dT 
) const
overridevirtual

Definition at line 124 of file MethaneFluidProperties.C.

126 {
127  // Check the temperature is in the range of validity (200 K <= T <= 1000 K)
128  if (temperature <= 200.0 || temperature >= 1000.0)
129  mooseException(
130  "Temperature ", temperature, "K out of range (200K, 1000K) in ", name(), ": k()");
131 
132  Real kt = 0.0, dkt_dT = 0.0;
133 
134  for (std::size_t i = 0; i < _b.size(); ++i)
135  kt += _b[i] * MathUtils::pow(temperature, i);
136 
137  for (std::size_t i = 1; i < _b.size(); ++i)
138  dkt_dT += i * _b[i] * MathUtils::pow(temperature, i) / temperature;
139 
140  k = kt;
141  dk_dp = 0.0;
142  dk_dT = dkt_dT;
143 }
static const std::string temperature
Definition: NS.h:57
virtual const std::string & name() const
const std::array< Real, 7 > _b
Coefficients for thermal conductivity.
DIE A HORRIBLE DEATH HERE typedef LIBMESH_DEFAULT_SCALAR_TYPE Real
T pow(T x, int e)
static const std::string k
Definition: NS.h:124

◆ makeZeroAndOne() [1/2]

template<typename T >
std::pair< T, T > SinglePhaseFluidProperties::makeZeroAndOne ( const T )
staticprotectedinherited

Given a type example, this method returns zero and unity reperesentations of that type (first and second members of returned pair respectively)

Definition at line 458 of file SinglePhaseFluidProperties.h.

Referenced by SinglePhaseFluidProperties::xyDerivatives().

459 {
460  return {T{0, 0}, T{1, 0}};
461 }

◆ makeZeroAndOne() [2/2]

template<>
std::pair<Real, Real> SinglePhaseFluidProperties::makeZeroAndOne ( const Real )
inlineinherited

Definition at line 465 of file SinglePhaseFluidProperties.h.

466 {
467  return {Real{0}, Real{1}};
468 }
DIE A HORRIBLE DEATH HERE typedef LIBMESH_DEFAULT_SCALAR_TYPE Real

◆ molarMass()

Real MethaneFluidProperties::molarMass ( ) const
overridevirtual

Fluid name.

Returns
string representing fluid name Molar mass [kg/mol]
molar mass

Reimplemented from SinglePhaseFluidProperties.

Definition at line 44 of file MethaneFluidProperties.C.

45 {
46  return _Mch4;
47 }
const Real _Mch4
Methane molar mass (kg/mol)

◆ mu_from_p_T() [1/2]

Real MethaneFluidProperties::mu_from_p_T ( Real  pressure,
Real  temperature 
) const
overridevirtual

Definition at line 80 of file MethaneFluidProperties.C.

Referenced by mu_from_p_T().

81 {
82  // Check the temperature is in the range of validity (200 K <= T <= 1000 K)
83  if (temperature <= 200.0 || temperature >= 1000.0)
84  mooseException(
85  "Temperature ", temperature, "K out of range (200K, 1000K) in ", name(), ": mu_from_p_T()");
86 
87  Real viscosity = 0.0;
88  for (std::size_t i = 0; i < _a.size(); ++i)
89  viscosity += _a[i] * MathUtils::pow(temperature, i);
90 
91  return viscosity * 1.e-6;
92 }
static const std::string temperature
Definition: NS.h:57
virtual const std::string & name() const
DIE A HORRIBLE DEATH HERE typedef LIBMESH_DEFAULT_SCALAR_TYPE Real
T pow(T x, int e)
const std::array< Real, 6 > _a
Coefficients for viscosity.

◆ mu_from_p_T() [2/2]

void MethaneFluidProperties::mu_from_p_T ( Real  pressure,
Real  temperature,
Real mu,
Real dmu_dp,
Real dmu_dT 
) const
overridevirtual

Definition at line 95 of file MethaneFluidProperties.C.

97 {
98 
100  dmu_dp = 0.0;
101 
102  Real dmudt = 0.0;
103  for (std::size_t i = 0; i < _a.size(); ++i)
104  dmudt += i * _a[i] * MathUtils::pow(temperature, i) / temperature;
105  dmu_dT = dmudt * 1.e-6;
106 }
virtual Real mu_from_p_T(Real pressure, Real temperature) const override
static const std::string temperature
Definition: NS.h:57
static const std::string mu
Definition: NS.h:122
DIE A HORRIBLE DEATH HERE typedef LIBMESH_DEFAULT_SCALAR_TYPE Real
static const std::string pressure
Definition: NS.h:56
T pow(T x, int e)
const std::array< Real, 6 > _a
Coefficients for viscosity.

◆ p_from_rho_T()

Real HelmholtzFluidProperties::p_from_rho_T ( Real  rho,
Real  T 
) const
virtualinherited

Pressure as a function of density and temperature.

Parameters
rhodensity (kg/m^3)
Ttemperature (K)
Returns
pressure (Pa)

Reimplemented in CO2FluidProperties.

Definition at line 220 of file HelmholtzFluidProperties.C.

Referenced by CO2FluidProperties::p_from_rho_T(), and HelmholtzFluidProperties::rho_from_p_T().

221 {
222  // Scale the input density and temperature
223  const Real delta = density / criticalDensity();
224  const Real tau = criticalTemperature() / temperature;
225 
226  return _R * density * temperature * delta * dalpha_ddelta(delta, tau) / molarMass();
227 }
virtual virtual std Real molarMass() const
Fluid name.
static const std::string density
Definition: NS.h:33
int delta(unsigned int i, unsigned int j)
Delta function, which returns zero if $i j$ and unity if $i=j$.
static const Real _R
Universal gas constant (J/mol/K)
static const std::string temperature
Definition: NS.h:57
virtual Real criticalTemperature() const
Critical temperature.
virtual Real dalpha_ddelta(Real delta, Real tau) const =0
Derivative of Helmholtz free energy wrt delta.
virtual Real criticalDensity() const
Critical density.
DIE A HORRIBLE DEATH HERE typedef LIBMESH_DEFAULT_SCALAR_TYPE Real

◆ p_T_from_h_s()

template<typename T >
void SinglePhaseFluidProperties::p_T_from_h_s ( const T h,
const T s,
Real  p0,
Real  T0,
T pressure,
T temperature,
bool &  conversion_succeeded 
) const
inherited

Determines (p,T) from (h,s) using Newton Solve in 2D Useful for conversion between different sets of state variables.

Parameters
[in]hspecific enthalpy (J / kg)
[in]sspecific entropy (J/K*kg)
[in]p0initial guess for pressure (Pa / kg)
[in]T0initial guess for temperature (K)
[out]fluidpressure (Pa / kg)
[out]Temperature(K)

Definition at line 557 of file SinglePhaseFluidProperties.h.

Referenced by TabulatedFluidProperties::T_from_h_s().

564 {
565  auto h_lambda = [&](const T & pressure, const T & temperature, T & new_h, T & dh_dp, T & dh_dT)
566  { h_from_p_T(pressure, temperature, new_h, dh_dp, dh_dT); };
567  auto s_lambda = [&](const T & pressure, const T & temperature, T & new_s, T & ds_dp, T & ds_dT)
568  { s_from_p_T(pressure, temperature, new_s, ds_dp, ds_dT); };
569  try
570  {
572  h, s, p0, T0, pressure, temperature, _tolerance, _tolerance, h_lambda, s_lambda);
573  conversion_succeeded = true;
574  }
575  catch (MooseException &)
576  {
577  conversion_succeeded = false;
578  }
579 
580  if (!conversion_succeeded)
581  mooseDoOnce(mooseWarning("Conversion from (h, s)=(", h, ", ", s, ") to (p, T) failed"));
582 }
static const std::string temperature
Definition: NS.h:57
void mooseWarning(Args &&... args) const
const Real _tolerance
Newton&#39;s method may be used to convert between variable sets _tolerance, _T_initial_guess, and _p_initial_guess are the parameters for these iterative solves.
void NewtonSolve2D(const T &f, const T &g, const Real x0, const Real y0, T &x_final, T &y_final, const Real f_tol, const Real g_tol, const Functor1 &func1, const Functor2 &func2, const unsigned int max_its=100)
NewtonSolve2D does a 2D Newton Solve to solve for the x and y such that: f = func1(x, y) and g = func2(x, y).
e e e e s T T T T T rho v v T h
static const std::string pressure
Definition: NS.h:56

◆ p_T_from_v_e()

template<typename CppType >
void SinglePhaseFluidProperties::p_T_from_v_e ( const CppType &  v,
const CppType &  e,
Real  p0,
Real  T0,
CppType &  p,
CppType &  T,
bool &  conversion_succeeded 
) const
inherited

Determines (p,T) from (v,e) using Newton Solve in 2D Useful for conversion between different sets of state variables.

Parameters
[in]vspecific volume (m^3 / kg)
[in]especific internal energy (J / kg)
[in]p0initial guess for pressure (Pa / kg)
[in]T0initial guess for temperature (K)
[out]fluidpressure (Pa / kg)
[out]Temperature(K)

Definition at line 493 of file SinglePhaseFluidProperties.h.

Referenced by TabulatedBicubicFluidProperties::constructInterpolation(), and TabulatedFluidProperties::g_from_v_e().

500 {
501  auto v_lambda = [&](const CppType & pressure,
502  const CppType & temperature,
503  CppType & new_v,
504  CppType & dv_dp,
505  CppType & dv_dT) { v_from_p_T(pressure, temperature, new_v, dv_dp, dv_dT); };
506  auto e_lambda = [&](const CppType & pressure,
507  const CppType & temperature,
508  CppType & new_e,
509  CppType & de_dp,
510  CppType & de_dT) { e_from_p_T(pressure, temperature, new_e, de_dp, de_dT); };
511  try
512  {
514  v, e, p0, T0, p, T, _tolerance, _tolerance, v_lambda, e_lambda);
515  conversion_succeeded = true;
516  }
517  catch (MooseException &)
518  {
519  conversion_succeeded = false;
520  }
521 
522  if (!conversion_succeeded)
523  mooseDoOnce(mooseWarning("Conversion from (v, e)=(", v, ", ", e, ") to (p, T) failed"));
524 }
static const std::string temperature
Definition: NS.h:57
void mooseWarning(Args &&... args) const
const Real _tolerance
Newton&#39;s method may be used to convert between variable sets _tolerance, _T_initial_guess, and _p_initial_guess are the parameters for these iterative solves.
void NewtonSolve2D(const T &f, const T &g, const Real x0, const Real y0, T &x_final, T &y_final, const Real f_tol, const Real g_tol, const Functor1 &func1, const Functor2 &func2, const unsigned int max_its=100)
NewtonSolve2D does a 2D Newton Solve to solve for the x and y such that: f = func1(x, y) and g = func2(x, y).
static const std::string pressure
Definition: NS.h:56

◆ p_T_from_v_h()

template<typename T >
void SinglePhaseFluidProperties::p_T_from_v_h ( const T v,
const T h,
Real  p0,
Real  T0,
T pressure,
T temperature,
bool &  conversion_succeeded 
) const
inherited

Determines (p,T) from (v,h) using Newton Solve in 2D Useful for conversion between different sets of state variables.

Parameters
[in]vspecific volume (m^3 / kg)
[in]hspecific enthalpy (J / kg)
[in]p0initial guess for pressure (Pa / kg)
[in]T0initial guess for temperature (K)
[out]fluidpressure (Pa / kg)
[out]Temperature(K)

Definition at line 528 of file SinglePhaseFluidProperties.h.

Referenced by TabulatedBicubicFluidProperties::constructInterpolation().

535 {
536  auto v_lambda = [&](const T & pressure, const T & temperature, T & new_v, T & dv_dp, T & dv_dT)
537  { v_from_p_T(pressure, temperature, new_v, dv_dp, dv_dT); };
538  auto h_lambda = [&](const T & pressure, const T & temperature, T & new_h, T & dh_dp, T & dh_dT)
539  { h_from_p_T(pressure, temperature, new_h, dh_dp, dh_dT); };
540  try
541  {
543  v, h, p0, T0, pressure, temperature, _tolerance, _tolerance, v_lambda, h_lambda);
544  conversion_succeeded = true;
545  }
546  catch (MooseException &)
547  {
548  conversion_succeeded = false;
549  }
550 
551  if (!conversion_succeeded)
552  mooseDoOnce(mooseWarning("Conversion from (v, h)=(", v, ", ", h, ") to (p, T) failed"));
553 }
static const std::string temperature
Definition: NS.h:57
void mooseWarning(Args &&... args) const
const Real _tolerance
Newton&#39;s method may be used to convert between variable sets _tolerance, _T_initial_guess, and _p_initial_guess are the parameters for these iterative solves.
void NewtonSolve2D(const T &f, const T &g, const Real x0, const Real y0, T &x_final, T &y_final, const Real f_tol, const Real g_tol, const Functor1 &func1, const Functor2 &func2, const unsigned int max_its=100)
NewtonSolve2D does a 2D Newton Solve to solve for the x and y such that: f = func1(x, y) and g = func2(x, y).
e e e e s T T T T T rho v v T h
static const std::string pressure
Definition: NS.h:56

◆ propfunc() [1/14]

SinglePhaseFluidProperties::propfunc ( p  ,
v  ,
 
)
inherited

Compute a fluid property given for the state defined by two given properties.

For all functions, the first two arguments are the given properties that define the fluid state. For the two-argument variants, the desired property is the return value. The five-argument variants also provide partial derivatives dx/da and dx/db where x is the desired property being computed, a is the first given property, and b is the second given property. The desired property, dx/da, and dx/db are stored into the 3rd, 4th, and 5th arguments respectively.

Properties/parameters used in these function are listed below with their units:

p pressure [Pa] T temperature [K] e specific internal energy [J/kg] v specific volume [m^3/kg] rho density [kg/m^3] h specific enthalpy [J/kg] s specific entropy [J/(kg*K)] mu viscosity [Pa*s] k thermal conductivity [W/(m*K)] c speed of sound [m/s] cp constant-pressure specific heat [J/K] cv constant-volume specific heat [J/K] beta volumetric thermal expansion coefficient [1/K] g Gibbs free energy [J] pp_sat partial pressure at saturation [Pa] gamma Adiabatic ratio (cp/cv) [-]

As an example:

// calculate pressure given specific vol and energy: auto pressure = your_fluid_properties_object.p_from_v_e(specific_vol, specific_energy);

// or use the derivative variant: Real dp_dv = 0; // derivative will be stored into here Real dp_de = 0; // derivative will be stored into here your_fluid_properties_object.p_from_v_e(specific_vol, specific_energy, pressure, dp_dv, dp_de);

Automatic differentiation (AD) support is provided through x_from_a_b(DualReal a, DualReal b) 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:

auto v = 1/rho; // rho must be an AD non-linear variable. auto e = rhoE/rho - vel_energy; // rhoE and vel_energy must be AD variables/numbers also. auto pressure = your_fluid_properties_object.p_from_v_e(v, e); // pressure now contains partial derivatives w.r.t. all degrees of freedom

◆ propfunc() [2/14]

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

◆ propfunc() [3/14]

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

◆ propfunc() [4/14]

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

◆ propfunc() [5/14]

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

◆ propfunc() [6/14]

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

◆ propfunc() [7/14]

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

◆ propfunc() [8/14]

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

◆ propfunc() [9/14]

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

◆ propfunc() [10/14]

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

◆ propfunc() [11/14]

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

◆ propfunc() [12/14]

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

◆ propfunc() [13/14]

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

◆ propfunc() [14/14]

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

◆ propfuncWithDefault() [1/4]

e e e e s T T T SinglePhaseFluidProperties::propfuncWithDefault ( cp  ,
p  ,
T   
)
inherited

◆ propfuncWithDefault() [2/4]

e e e e s T T T T SinglePhaseFluidProperties::propfuncWithDefault ( mu  ,
p  ,
T   
)
inherited

◆ propfuncWithDefault() [3/4]

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

◆ propfuncWithDefault() [4/4]

e e e e s T T T T T rho v v T s h T SinglePhaseFluidProperties::propfuncWithDefault ( ,
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 413 of file SinglePhaseFluidProperties.C.

421 {
422  rho_from_p_T(p, T, rho, drho_dp, drho_dT);
423  e_from_p_T(p, T, e, de_dp, de_dT);
424 }

◆ rho_from_p_T() [1/2]

Real HelmholtzFluidProperties::rho_from_p_T ( Real  pressure,
Real  temperature 
) const
overridevirtualinherited

Reimplemented in CO2FluidProperties.

Definition at line 28 of file HelmholtzFluidProperties.C.

Referenced by HelmholtzFluidProperties::c_from_p_T(), HelmholtzFluidProperties::cp_from_p_T(), HelmholtzFluidProperties::cv_from_p_T(), HelmholtzFluidProperties::e_from_p_T(), HelmholtzFluidProperties::h_from_p_T(), NitrogenFluidProperties::k_from_p_T(), HydrogenFluidProperties::k_from_p_T(), NitrogenFluidProperties::mu_from_p_T(), CO2FluidProperties::mu_from_p_T(), HydrogenFluidProperties::mu_from_p_T(), HelmholtzFluidProperties::rho_from_p_T(), CO2FluidProperties::rho_from_p_T(), NitrogenFluidProperties::rho_mu_from_p_T(), HydrogenFluidProperties::rho_mu_from_p_T(), and HelmholtzFluidProperties::s_from_p_T().

29 {
30  Real density;
31  // Initial estimate of a bracketing interval for the density
32  Real lower_density = 1.0e-2;
33  Real upper_density = 100.0;
34 
35  // The density is found by finding the zero of the pressure
36  auto pressure_diff = [&pressure, &temperature, this](Real x)
37  { return this->p_from_rho_T(x, temperature) - pressure; };
38 
39  BrentsMethod::bracket(pressure_diff, lower_density, upper_density);
40  density = BrentsMethod::root(pressure_diff, lower_density, upper_density);
41 
42  return density;
43 }
static const std::string density
Definition: NS.h:33
static const std::string temperature
Definition: NS.h:57
const std::vector< double > x
Real root(std::function< Real(Real)> const &f, Real x1, Real x2, Real tol=1.0e-12)
Finds the root of a function using Brent&#39;s method.
Definition: BrentsMethod.C:61
virtual Real p_from_rho_T(Real rho, Real T) const
Pressure as a function of density and temperature.
DIE A HORRIBLE DEATH HERE typedef LIBMESH_DEFAULT_SCALAR_TYPE Real
static const std::string pressure
Definition: NS.h:56
void bracket(std::function< Real(Real)> const &f, Real &x1, Real &x2)
Function to bracket a root of a given function.
Definition: BrentsMethod.C:17

◆ rho_from_p_T() [2/2]

void HelmholtzFluidProperties::rho_from_p_T ( Real  pressure,
Real  temperature,
Real rho,
Real drho_dp,
Real drho_dT 
) const
overridevirtualinherited

Reimplemented in CO2FluidProperties.

Definition at line 46 of file HelmholtzFluidProperties.C.

48 {
50 
51  // Scale the density and temperature
52  const Real delta = rho / criticalDensity();
53  const Real tau = criticalTemperature() / temperature;
54  const Real da_dd = dalpha_ddelta(delta, tau);
55  const Real d2a_dd2 = d2alpha_ddelta2(delta, tau);
56 
57  drho_dp = molarMass() / (_R * temperature * delta * (2.0 * da_dd + delta * d2a_dd2));
58  drho_dT = rho * (tau * d2alpha_ddeltatau(delta, tau) - da_dd) / temperature /
59  (2.0 * da_dd + delta * d2a_dd2);
60 }
virtual Real d2alpha_ddeltatau(Real delta, Real tau) const =0
Second derivative of Helmholtz free energy wrt delta and tau.
virtual virtual std Real molarMass() const
Fluid name.
int delta(unsigned int i, unsigned int j)
Delta function, which returns zero if $i j$ and unity if $i=j$.
static const Real _R
Universal gas constant (J/mol/K)
static const std::string temperature
Definition: NS.h:57
virtual Real d2alpha_ddelta2(Real delta, Real tau) const =0
Second derivative of Helmholtz free energy wrt delta.
virtual Real criticalTemperature() const
Critical temperature.
virtual Real dalpha_ddelta(Real delta, Real tau) const =0
Derivative of Helmholtz free energy wrt delta.
virtual Real rho_from_p_T(Real pressure, Real temperature) const override
virtual Real criticalDensity() const
Critical density.
DIE A HORRIBLE DEATH HERE typedef LIBMESH_DEFAULT_SCALAR_TYPE Real
static const std::string pressure
Definition: NS.h:56

◆ rho_mu_from_p_T() [1/3]

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 property names are described above.

Reimplemented in Water97FluidProperties, CO2FluidProperties, HydrogenFluidProperties, and NitrogenFluidProperties.

Definition at line 427 of file SinglePhaseFluidProperties.C.

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

428 {
429  rho = rho_from_p_T(p, T);
430  mu = mu_from_p_T(p, T);
431 }
static const std::string mu
Definition: NS.h:122

◆ 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 434 of file SinglePhaseFluidProperties.C.

442 {
443  rho_from_p_T(p, T, rho, drho_dp, drho_dT);
444  mu_from_p_T(p, T, mu, dmu_dp, dmu_dT);
445 }
static const std::string mu
Definition: NS.h:122

◆ rho_mu_from_p_T() [3/3]

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

Definition at line 448 of file SinglePhaseFluidProperties.C.

452 {
453  rho = rho_from_p_T(p, T);
454  mu = mu_from_p_T(p, T);
455 }
static const std::string mu
Definition: NS.h:122

◆ s_from_p_T() [1/2]

Real HelmholtzFluidProperties::s_from_p_T ( Real  pressure,
Real  temperature 
) const
overridevirtualinherited

Definition at line 148 of file HelmholtzFluidProperties.C.

Referenced by HelmholtzFluidProperties::s_from_p_T().

149 {
150  // Require density first
152  // Scale the input density and temperature
153  const Real delta = density / criticalDensity();
154  const Real tau = criticalTemperature() / temperature;
155 
156  return _R * (tau * dalpha_dtau(delta, tau) - alpha(delta, tau)) / molarMass();
157 }
virtual virtual std Real molarMass() const
Fluid name.
static const std::string density
Definition: NS.h:33
int delta(unsigned int i, unsigned int j)
Delta function, which returns zero if $i j$ and unity if $i=j$.
static const Real _R
Universal gas constant (J/mol/K)
static const std::string temperature
Definition: NS.h:57
virtual Real criticalTemperature() const
Critical temperature.
virtual Real rho_from_p_T(Real pressure, Real temperature) const override
virtual Real dalpha_dtau(Real delta, Real tau) const =0
Derivative of Helmholtz free energy wrt tau.
virtual Real alpha(Real delta, Real tau) const =0
Helmholtz free energy.
virtual Real criticalDensity() const
Critical density.
DIE A HORRIBLE DEATH HERE typedef LIBMESH_DEFAULT_SCALAR_TYPE Real
static const std::string pressure
Definition: NS.h:56

◆ s_from_p_T() [2/2]

void HelmholtzFluidProperties::s_from_p_T ( Real  p,
Real  T,
Real s,
Real ds_dp,
Real ds_dT 
) const
overridevirtualinherited

Definition at line 160 of file HelmholtzFluidProperties.C.

162 {
163  s = this->s_from_p_T(pressure, temperature);
164 
165  // Require density first
167  // Scale the input density and temperature
168  const Real delta = density / criticalDensity();
169  const Real tau = criticalTemperature() / temperature;
170 
171  const Real da_dd = dalpha_ddelta(delta, tau);
172  const Real da_dt = dalpha_dtau(delta, tau);
173  const Real d2a_dd2 = d2alpha_ddelta2(delta, tau);
174  const Real d2a_dt2 = d2alpha_dtau2(delta, tau);
175  const Real d2a_ddt = d2alpha_ddeltatau(delta, tau);
176 
177  ds_dp = tau * (d2a_ddt - da_dd) / (density * temperature * (2.0 * da_dd + delta * d2a_dd2));
178  ds_dT = -_R * tau * (da_dt - alpha(delta, tau) + tau * (d2a_dt2 - da_dt)) /
179  (molarMass() * temperature);
180 }
virtual Real d2alpha_ddeltatau(Real delta, Real tau) const =0
Second derivative of Helmholtz free energy wrt delta and tau.
virtual Real d2alpha_dtau2(Real delta, Real tau) const =0
Second derivative of Helmholtz free energy wrt tau.
virtual virtual std Real molarMass() const
Fluid name.
static const std::string density
Definition: NS.h:33
int delta(unsigned int i, unsigned int j)
Delta function, which returns zero if $i j$ and unity if $i=j$.
static const Real _R
Universal gas constant (J/mol/K)
static const std::string temperature
Definition: NS.h:57
virtual Real d2alpha_ddelta2(Real delta, Real tau) const =0
Second derivative of Helmholtz free energy wrt delta.
virtual Real criticalTemperature() const
Critical temperature.
virtual Real dalpha_ddelta(Real delta, Real tau) const =0
Derivative of Helmholtz free energy wrt delta.
virtual Real rho_from_p_T(Real pressure, Real temperature) const override
virtual Real dalpha_dtau(Real delta, Real tau) const =0
Derivative of Helmholtz free energy wrt tau.
virtual Real alpha(Real delta, Real tau) const =0
Helmholtz free energy.
virtual Real criticalDensity() const
Critical density.
DIE A HORRIBLE DEATH HERE typedef LIBMESH_DEFAULT_SCALAR_TYPE Real
virtual Real s_from_p_T(Real pressure, Real temperature) const override
static const std::string pressure
Definition: NS.h:56

◆ saturatedLiquidDensity()

Real MethaneFluidProperties::saturatedLiquidDensity ( Real  temperature) const

Saturated liquid density of CH4 Valid for temperatures between the triple point temperature and critical temperature.

Eq. (3.4), from Setzmann and Wagner (reference above)

Parameters
temperaturetemperature (K)
Returns
saturated liquid density (kg/m^3)

Definition at line 174 of file MethaneFluidProperties.C.

175 {
176  if (temperature < _T_triple || temperature > _T_critical)
177  mooseException(
178  "Temperature ", temperature, " is out of range in ", name(), ": saturatedLiquidDensity()");
179 
180  const Real Tr = temperature / _T_critical;
181  const Real theta = 1.0 - Tr;
182 
183  const Real logdensity = 1.9906389 * std::pow(theta, 0.354) - 0.78756197 * std::sqrt(theta) +
184  0.036976723 * std::pow(theta, 2.5);
185 
186  return _rho_critical * std::exp(logdensity);
187 }
static const std::string temperature
Definition: NS.h:57
ADRealEigenVector< T, D, asd > sqrt(const ADRealEigenVector< T, D, asd > &)
virtual const std::string & name() const
DIE A HORRIBLE DEATH HERE typedef LIBMESH_DEFAULT_SCALAR_TYPE Real
const Real _rho_critical
Critical density (kg/m^3)
const Real _T_critical
Critical temperature (K)
MooseUnits pow(const MooseUnits &, int)

◆ saturatedVaporDensity()

Real MethaneFluidProperties::saturatedVaporDensity ( Real  temperature) const

Saturated vapor density of CH4 Valid for temperatures between the triple point temperature and critical temperature.

Eq. (3.5), from Setzmann and Wagner (reference above)

Parameters
temperaturetemperature (K)
Returns
saturated vapor density (kg/m^3)

Definition at line 190 of file MethaneFluidProperties.C.

191 {
192  if (temperature < _T_triple || temperature > _T_critical)
193  mooseException(
194  "Temperature ", temperature, " is out of range in ", name(), ": saturatedVaporDensity()");
195 
196  const Real Tr = temperature / _T_critical;
197  const Real theta = 1.0 - Tr;
198 
199  const Real logdensity =
200  -1.880284 * std::pow(theta, 0.354) - 2.8526531 * std::pow(theta, 5.0 / 6.0) -
201  3.000648 * std::pow(theta, 1.5) - 5.251169 * std::pow(theta, 2.5) -
202  13.191859 * std::pow(theta, 25.0 / 6.0) - 37.553961 * std::pow(theta, 47.0 / 6.0);
203 
204  return _rho_critical * std::exp(logdensity);
205 }
static const std::string temperature
Definition: NS.h:57
virtual const std::string & name() const
DIE A HORRIBLE DEATH HERE typedef LIBMESH_DEFAULT_SCALAR_TYPE Real
const Real _rho_critical
Critical density (kg/m^3)
const Real _T_critical
Critical temperature (K)
MooseUnits pow(const MooseUnits &, int)

◆ subdomainSetup()

virtual void FluidProperties::subdomainSetup ( )
inlinefinalvirtualinherited

Reimplemented from ThreadedGeneralUserObject.

Definition at line 38 of file FluidProperties.h.

38 {}

◆ threadJoin()

virtual void FluidProperties::threadJoin ( const UserObject )
inlinefinalvirtualinherited

Reimplemented from ThreadedGeneralUserObject.

Definition at line 37 of file FluidProperties.h.

37 {}

◆ triplePointPressure()

Real MethaneFluidProperties::triplePointPressure ( ) const
overridevirtual

Triple point pressure.

Returns
triple point pressure (Pa)

Reimplemented from SinglePhaseFluidProperties.

Definition at line 68 of file MethaneFluidProperties.C.

69 {
70  return _p_triple;
71 }
const Real _p_triple
Triple point pressure (Pa)

◆ triplePointTemperature()

Real MethaneFluidProperties::triplePointTemperature ( ) const
overridevirtual

Triple point temperature.

Returns
triple point temperature (K)

Reimplemented from SinglePhaseFluidProperties.

Definition at line 74 of file MethaneFluidProperties.C.

75 {
76  return _T_triple;
77 }
const Real _T_triple
Triple point temperature (K)

◆ v_e_from_p_T() [1/2]

template<typename CppType >
void SinglePhaseFluidProperties::v_e_from_p_T ( const CppType &  p,
const CppType &  T,
CppType &  v,
CppType &  e 
) const
inherited

Definition at line 586 of file SinglePhaseFluidProperties.h.

590 {
591  const CppType rho = rho_from_p_T(p, T);
592  v = 1.0 / rho;
593  try
594  {
595  // more likely to not involve a Newton search
596  e = e_from_p_T(p, T);
597  }
598  catch (...)
599  {
600  e = e_from_p_rho(p, rho);
601  }
602 }

◆ v_e_from_p_T() [2/2]

template<typename CppType >
void SinglePhaseFluidProperties::v_e_from_p_T ( const CppType &  p,
const CppType &  T,
CppType &  v,
CppType &  dv_dp,
CppType &  dv_dT,
CppType &  e,
CppType &  de_dp,
CppType &  de_dT 
) const
inherited

Definition at line 606 of file SinglePhaseFluidProperties.h.

614 {
615  CppType rho, drho_dp, drho_dT;
616  rho_from_p_T(p, T, rho, drho_dp, drho_dT);
617 
618  v = 1.0 / rho;
619  const CppType dv_drho = -1.0 / (rho * rho);
620  dv_dp = dv_drho * drho_dp;
621  dv_dT = dv_drho * drho_dT;
622 
623  CppType de_dp_partial, de_drho;
624  e_from_p_rho(p, rho, e, de_dp_partial, de_drho);
625  de_dp = de_dp_partial + de_drho * drho_dp;
626  de_dT = de_drho * drho_dT;
627 }

◆ 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]Ttemperature
[in]vspecific volume

Reimplemented in IdealGasFluidProperties, CaloricallyImperfectGas, and StiffenedGasFluidProperties.

Definition at line 463 of file SinglePhaseFluidProperties.C.

Referenced by IdealRealGasMixtureFluidProperties::v_from_p_T().

464 {
465  mooseError(__PRETTY_FUNCTION__, " not implemented.");
466 }
void mooseError(Args &&... args) const

◆ validParams()

InputParameters MethaneFluidProperties::validParams ( )
static

Definition at line 17 of file MethaneFluidProperties.C.

18 {
20  params.addClassDescription("Fluid properties for methane (CH4)");
21  return params;
22 }
static InputParameters validParams()
void addClassDescription(const std::string &doc_string)

◆ vaporPressure() [1/3]

Real MethaneFluidProperties::vaporPressure ( Real  T) const
overridevirtual

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 from SinglePhaseFluidProperties.

Definition at line 146 of file MethaneFluidProperties.C.

147 {
148  if (temperature < _T_triple || temperature > _T_critical)
149  mooseException("Temperature is out of range in ", name(), ": vaporPressure()");
150 
151  const Real Tr = temperature / _T_critical;
152  const Real theta = 1.0 - Tr;
153 
154  const Real logpressure = (-6.036219 * theta + 1.409353 * std::pow(theta, 1.5) -
155  0.4945199 * Utility::pow<2>(theta) - 1.443048 * std::pow(theta, 4.5)) /
156  Tr;
157 
158  return _p_critical * std::exp(logpressure);
159 }
static const std::string temperature
Definition: NS.h:57
virtual const std::string & name() const
DIE A HORRIBLE DEATH HERE typedef LIBMESH_DEFAULT_SCALAR_TYPE Real
const Real _T_critical
Critical temperature (K)
const Real _p_critical
Critical pressure (Pa)
MooseUnits pow(const MooseUnits &, int)

◆ vaporPressure() [2/3]

void MethaneFluidProperties::vaporPressure ( Real  temperature,
Real psat,
Real dpsat_dT 
) const
overridevirtual

Reimplemented from SinglePhaseFluidProperties.

Definition at line 162 of file MethaneFluidProperties.C.

163 {
164  mooseError("vaporPressure() is not implemented");
165 }
void mooseError(Args &&... args) const

◆ vaporPressure() [3/3]

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

Definition at line 369 of file SinglePhaseFluidProperties.C.

370 {
371  Real p = 0.0;
372  Real temperature = T.value();
373  Real dpdT = 0.0;
374 
375  vaporPressure(temperature, p, dpdT);
376 
377  DualReal result = p;
378  result.derivatives() = T.derivatives() * dpdT;
379 
380  return result;
381 }
DualNumber< Real, DNDerivativeType, true > DualReal
static const std::string temperature
Definition: NS.h:57
DIE A HORRIBLE DEATH HERE typedef LIBMESH_DEFAULT_SCALAR_TYPE Real
virtual Real vaporPressure(Real T) const
Vapor pressure.

◆ vaporTemperature() [1/3]

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

Reimplemented in Water97FluidProperties.

Definition at line 383 of file SinglePhaseFluidProperties.C.

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

384 {
385  mooseError(__PRETTY_FUNCTION__, " not implemented.");
386 }
void mooseError(Args &&... args) const

◆ vaporTemperature() [2/3]

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

Reimplemented in Water97FluidProperties.

Definition at line 389 of file SinglePhaseFluidProperties.C.

390 {
391  fluidPropError(__PRETTY_FUNCTION__, " derivatives not implemented.");
392 
393  dT_dp = 0.0;
394  T = vaporTemperature(p);
395 }
virtual Real vaporTemperature(Real p) const
Vapor temperature.
void fluidPropError(Args... args) const

◆ vaporTemperature() [3/3]

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

Definition at line 398 of file SinglePhaseFluidProperties.C.

399 {
400  Real T = 0.0;
401  Real pressure = p.value();
402  Real dTdp = 0.0;
403 
404  vaporTemperature(pressure, T, dTdp);
405 
406  DualReal result = T;
407  result.derivatives() = p.derivatives() * dTdp;
408 
409  return result;
410 }
DualNumber< Real, DNDerivativeType, true > DualReal
virtual Real vaporTemperature(Real p) const
Vapor temperature.
DIE A HORRIBLE DEATH HERE typedef LIBMESH_DEFAULT_SCALAR_TYPE Real
static const std::string pressure
Definition: NS.h:56

◆ xyDerivatives()

template<typename T , typename Functor >
void SinglePhaseFluidProperties::xyDerivatives ( const T  x,
const T y,
T z,
T dz_dx,
T dz_dy,
const Functor z_from_x_y 
)
staticprotectedinherited

Computes the dependent variable z and its derivatives with respect to the independent variables x and y using the simple two parameter z_from_x_y functor.

The derivatives are computed using a compound automatic differentiation type

Definition at line 472 of file SinglePhaseFluidProperties.h.

Referenced by Water97FluidProperties::e_from_p_rho_template(), Water97FluidProperties::h_from_p_T_template(), Water97FluidProperties::rho_from_p_T_template(), and Water97FluidProperties::v_from_p_T_template().

474 {
476  const auto [zero, one] = makeZeroAndOne(x);
477 
478  CompoundType x_c(x, zero);
479  auto & x_cd = x_c.derivatives();
480  x_cd[0] = one;
481  CompoundType y_c(y, zero);
482  auto & y_cd = y_c.derivatives();
483  y_cd[1] = one;
484 
485  const auto z_c = z_from_x_y(x_c, y_c);
486  z = z_c.value();
487  dz_dx = z_c.derivatives()[0];
488  dz_dy = z_c.derivatives()[1];
489 }
static std::pair< T, T > makeZeroAndOne(const T &)
Given a type example, this method returns zero and unity reperesentations of that type (first and sec...
const std::vector< double > y
const Number zero
const std::vector< double > x

Member Data Documentation

◆ _a

const std::array<Real, 6> MethaneFluidProperties::_a
protected
Initial value:
{
{2.968267e-1, 3.711201e-2, 1.218298e-5, -7.02426e-8, 7.543269e-11, -2.7237166e-14}}

Coefficients for viscosity.

Definition at line 166 of file MethaneFluidProperties.h.

Referenced by mu_from_p_T().

◆ _a0

const std::array<Real, 5> MethaneFluidProperties::_a0 {{0.008449, 4.6942, 3.4865, 1.6572, 1.4115}}
protected

Coefficients for ideal gas component of the Helmholtz free energy.

Definition at line 121 of file MethaneFluidProperties.h.

Referenced by alpha(), d2alpha_dtau2(), and dalpha_dtau().

◆ _allow_imperfect_jacobians

const bool FluidProperties::_allow_imperfect_jacobians
protectedinherited

Flag to set unimplemented Jacobian entries to zero.

Definition at line 47 of file FluidProperties.h.

Referenced by VaporMixtureFluidProperties::fluidPropError(), and SinglePhaseFluidProperties::fluidPropError().

◆ _alpha3

const std::array<Real, 4> MethaneFluidProperties::_alpha3 {{20.0, 40.0, 40.0, 40.0}}
protected

◆ _b

const std::array<Real, 7> MethaneFluidProperties::_b
protected
Initial value:
{{-1.3401499e-2,
3.663076e-4,
-1.82248608e-6,
5.93987998e-9,
-9.1405505e-12,
6.7896889e-15,
-1.95048736e-18}}

Coefficients for thermal conductivity.

Definition at line 169 of file MethaneFluidProperties.h.

Referenced by k_from_p_T().

◆ _b0

const std::array<Real, 5> MethaneFluidProperties::_b0 {{3.4004324, 10.26951575, 20.43932747, 29.93744884, 79.13351945}}
protected

Definition at line 122 of file MethaneFluidProperties.h.

Referenced by alpha(), d2alpha_dtau2(), and dalpha_dtau().

◆ _beta3

const std::array<Real, 4> MethaneFluidProperties::_beta3 {{200.0, 250.0, 250.0, 250.0}}
protected

◆ _c2

const std::array<unsigned int, 23> MethaneFluidProperties::_c2
protected
Initial value:
{
{1, 1, 1, 1, 1, 1, 1, 2, 2, 2, 2, 2, 3, 3, 3, 3, 4, 4, 4, 4, 4, 4, 4}}

Definition at line 151 of file MethaneFluidProperties.h.

Referenced by alpha(), d2alpha_ddelta2(), d2alpha_ddeltatau(), d2alpha_dtau2(), dalpha_ddelta(), and dalpha_dtau().

◆ _d1

const std::array<unsigned int, 13> MethaneFluidProperties::_d1 {{1, 1, 1, 2, 2, 2, 2, 3, 4, 4, 8, 9, 10}}
protected

◆ _d2

const std::array<unsigned int, 23> MethaneFluidProperties::_d2
protected
Initial value:
{
{1, 1, 1, 2, 4, 5, 6, 1, 2, 3, 4, 4, 3, 5, 5, 8, 2, 3, 4, 4, 4, 5, 6}}

Definition at line 153 of file MethaneFluidProperties.h.

Referenced by alpha(), d2alpha_ddelta2(), d2alpha_ddeltatau(), d2alpha_dtau2(), dalpha_ddelta(), and dalpha_dtau().

◆ _d3

const std::array<int, 4> MethaneFluidProperties::_d3 {{2, 0, 0, 0}}
protected

◆ _D3

const std::array<Real, 4> MethaneFluidProperties::_D3 {{1.0, 1.0, 1.0, 1.0}}
protected

◆ _gamma3

const std::array<Real, 4> MethaneFluidProperties::_gamma3 {{1.07, 1.11, 1.11, 1.11}}
protected

◆ _Mch4

const Real MethaneFluidProperties::_Mch4
protected

Methane molar mass (kg/mol)

Definition at line 108 of file MethaneFluidProperties.h.

Referenced by molarMass().

◆ _N1

const std::array<Real, 13> MethaneFluidProperties::_N1
protected
Initial value:
{{0.4367901028e-1,
0.6709236199,
-0.1765577859e1,
0.8582330241,
-0.1206513052e1,
0.512046722,
-0.4000010791e-3,
-0.1247842423e-1,
0.3100269701e-1,
0.1754748522e-2,
-0.3171921605e-5,
-0.224034684e-5,
0.2947056156e-6}}

Coefficients for residual component of the Helmholtz free energy.

Definition at line 125 of file MethaneFluidProperties.h.

Referenced by alpha(), d2alpha_ddelta2(), d2alpha_ddeltatau(), d2alpha_dtau2(), dalpha_ddelta(), and dalpha_dtau().

◆ _N2

const std::array<Real, 23> MethaneFluidProperties::_N2
protected
Initial value:
{
{0.1830487909, 0.1511883679, -0.4289363877, 0.6894002446e-1, -0.1408313996e-1,
-0.306305483e-1, -0.2969906708e-1, -0.1932040831e-1, -0.1105739959, 0.9952548995e-1,
0.8548437825e-2, -0.6150555662e-1, -0.4291792423e-1, -0.181320729e-1, 0.344590476e-1,
-0.238591945e-2, -0.1159094939e-1, 0.6641693602e-1, -0.237154959e-1, -0.3961624905e-1,
-0.1387292044e-1, 0.3389489599e-1, -0.2927378753e-2}}

Definition at line 142 of file MethaneFluidProperties.h.

Referenced by alpha(), d2alpha_ddelta2(), d2alpha_ddeltatau(), d2alpha_dtau2(), dalpha_ddelta(), and dalpha_dtau().

◆ _N3

const std::array<Real, 4> MethaneFluidProperties::_N3
protected
Initial value:
{
{0.9324799946e-4, -0.6287171518e1, 0.1271069467e2, -0.6423953466e1}}

Definition at line 156 of file MethaneFluidProperties.h.

Referenced by alpha(), d2alpha_ddelta2(), d2alpha_ddeltatau(), d2alpha_dtau2(), dalpha_ddelta(), and dalpha_dtau().

◆ _p_critical

const Real MethaneFluidProperties::_p_critical
protected

Critical pressure (Pa)

Definition at line 110 of file MethaneFluidProperties.h.

Referenced by criticalPressure(), and vaporPressure().

◆ _p_initial_guess

const Real SinglePhaseFluidProperties::_p_initial_guess
protectedinherited

◆ _p_triple

const Real MethaneFluidProperties::_p_triple
protected

Triple point pressure (Pa)

Definition at line 116 of file MethaneFluidProperties.h.

Referenced by triplePointPressure().

◆ _R

const Real FluidProperties::_R = 8.3144598
staticinherited

◆ _rho_critical

const Real MethaneFluidProperties::_rho_critical
protected

Critical density (kg/m^3)

Definition at line 114 of file MethaneFluidProperties.h.

Referenced by criticalDensity(), saturatedLiquidDensity(), and saturatedVaporDensity().

◆ _t1

const std::array<Real, 13> MethaneFluidProperties::_t1
protected
Initial value:
{
{-0.5, 0.5, 1.0, 0.5, 1.0, 1.5, 4.5, 0.0, 1.0, 3.0, 1.0, 3.0, 3.0}}

Definition at line 138 of file MethaneFluidProperties.h.

Referenced by alpha(), d2alpha_ddelta2(), d2alpha_ddeltatau(), d2alpha_dtau2(), dalpha_ddelta(), and dalpha_dtau().

◆ _t2

const std::array<Real, 23> MethaneFluidProperties::_t2
protected
Initial value:
{{0.0, 1.0, 2.0, 0.0, 0.0, 2.0, 2.0, 5.0,
5.0, 5.0, 2.0, 4.0, 12.0, 8.0, 10.0, 10.0,
10.0, 14.0, 12.0, 18.0, 22.0, 18.0, 14.0}}

Definition at line 148 of file MethaneFluidProperties.h.

Referenced by alpha(), d2alpha_ddelta2(), d2alpha_ddeltatau(), d2alpha_dtau2(), dalpha_ddelta(), and dalpha_dtau().

◆ _t3

const std::array<Real, 4> MethaneFluidProperties::_t3 {{2.0, 0.0, 1.0, 2.0}}
protected

◆ _T_c2k

const Real FluidProperties::_T_c2k
protectedinherited

◆ _T_critical

const Real MethaneFluidProperties::_T_critical
protected

Critical temperature (K)

Definition at line 112 of file MethaneFluidProperties.h.

Referenced by criticalTemperature(), saturatedLiquidDensity(), saturatedVaporDensity(), and vaporPressure().

◆ _T_initial_guess

const Real SinglePhaseFluidProperties::_T_initial_guess
protectedinherited

◆ _T_triple

const Real MethaneFluidProperties::_T_triple
protected

Triple point temperature (K)

Definition at line 118 of file MethaneFluidProperties.h.

Referenced by triplePointTemperature().

◆ _tolerance

const Real SinglePhaseFluidProperties::_tolerance
protectedinherited

◆ h

e e e e s T T T T T rho v v T SinglePhaseFluidProperties::h
inherited

Definition at line 205 of file SinglePhaseFluidProperties.h.

Referenced by SodiumSaturationFluidProperties::e_from_p_T(), NaKFluidProperties::e_from_p_T(), NaClFluidProperties::e_from_p_T(), LeadBismuthFluidProperties::e_from_p_T(), LeadFluidProperties::e_from_p_T(), CaloricallyImperfectGas::e_from_v_h(), StiffenedGasFluidProperties::e_from_v_h(), IdealGasFluidProperties::e_from_v_h(), Water97FluidProperties::e_from_v_h(), TabulatedFluidProperties::e_from_v_h(), SimpleFluidProperties::e_from_v_h(), TabulatedFluidProperties::g_from_v_e(), SodiumSaturationFluidProperties::h_from_p_T(), LinearFluidProperties::h_from_p_T(), HelmholtzFluidProperties::h_from_p_T(), StiffenedGasFluidProperties::h_from_p_T(), NaKFluidProperties::h_from_p_T(), TabulatedFluidProperties::h_from_p_T(), LeadBismuthFluidProperties::h_from_p_T(), LeadFluidProperties::h_from_p_T(), CaloricallyImperfectGas::h_from_p_T(), NaClFluidProperties::h_from_p_T(), IdealGasFluidProperties::h_from_p_T(), SimpleFluidProperties::h_from_p_T(), TemperaturePressureFunctionFluidProperties::h_from_p_T(), Water97FluidProperties::h_from_p_T(), FlibeFluidProperties::h_from_p_T(), FlinakFluidProperties::h_from_p_T(), HeliumFluidProperties::h_from_p_T(), Water97FluidProperties::h_from_p_T_template(), StiffenedGasFluidProperties::h_from_T_v(), CaloricallyImperfectGas::h_from_T_v(), IdealGasFluidProperties::h_from_T_v(), LeadBismuthFluidProperties::h_from_v_e(), LeadFluidProperties::h_from_v_e(), StiffenedGasFluidProperties::p_from_h_s(), IdealGasFluidProperties::p_from_h_s(), CaloricallyImperfectGas::p_from_h_s(), LeadBismuthFluidProperties::p_from_v_e(), LeadFluidProperties::p_from_v_e(), SimpleFluidProperties::p_from_v_h(), SinglePhaseFluidProperties::p_T_from_h_s(), SinglePhaseFluidProperties::p_T_from_v_h(), Water97FluidProperties::p_T_from_v_h(), StiffenedGasFluidProperties::s_from_h_p(), CaloricallyImperfectGas::s_from_h_p(), IdealGasFluidProperties::s_from_h_p(), TabulatedFluidProperties::s_from_h_p(), CaloricallyImperfectGas::T_from_h(), TabulatedFluidProperties::T_from_h_p(), TabulatedFluidProperties::T_from_h_s(), LeadBismuthFluidProperties::T_from_p_h(), LeadFluidProperties::T_from_p_h(), TemperaturePressureFunctionFluidProperties::T_from_p_h(), CaloricallyImperfectGas::T_from_p_h(), FlibeFluidProperties::T_from_p_h(), FlinakFluidProperties::T_from_p_h(), HeliumFluidProperties::T_from_p_h(), IdealGasFluidProperties::T_from_p_h(), SimpleFluidProperties::T_from_p_h(), Water97FluidProperties::T_from_p_h(), and SimpleFluidProperties::T_from_v_h().

◆ p [1/9]

e e e e SinglePhaseFluidProperties::p
inherited

Definition at line 185 of file SinglePhaseFluidProperties.h.

Referenced by LinearFluidProperties::beta_from_p_T(), CaloricallyImperfectGas::c_from_p_T(), Water97FluidProperties::c_from_p_T(), StiffenedGasFluidProperties::c_from_v_e(), HeliumFluidProperties::c_from_v_e(), TabulatedFluidProperties::c_from_v_e(), Water97FluidProperties::c_from_v_e(), SimpleFluidProperties::c_from_v_e(), LeadBismuthFluidProperties::cp_from_p_T(), LeadFluidProperties::cp_from_p_T(), IdealGasFluidProperties::cp_from_p_T(), TemperaturePressureFunctionFluidProperties::cp_from_p_T(), TemperaturePressureFunctionFluidProperties::cp_from_v_e(), TabulatedFluidProperties::cp_from_v_e(), Water97FluidProperties::cp_from_v_e(), LeadFluidProperties::cv_from_p_T(), LeadBismuthFluidProperties::cv_from_p_T(), IdealGasFluidProperties::cv_from_p_T(), LeadBismuthFluidProperties::cv_from_v_e(), LeadFluidProperties::cv_from_v_e(), TabulatedFluidProperties::cv_from_v_e(), Water97FluidProperties::cv_from_v_e(), TestSinglePhaseFluidProperties::e_from_p_rho(), LinearTestFluidProperties::e_from_p_rho(), LinearFluidProperties::e_from_p_rho(), IdealGasFluidProperties::e_from_p_rho(), LeadBismuthFluidProperties::e_from_p_rho(), LeadFluidProperties::e_from_p_rho(), Water97FluidProperties::e_from_p_rho(), SimpleFluidProperties::e_from_p_rho(), TemperaturePressureFunctionFluidProperties::e_from_p_rho(), FlibeFluidProperties::e_from_p_rho(), FlinakFluidProperties::e_from_p_rho(), HeliumFluidProperties::e_from_p_rho(), Water97FluidProperties::e_from_p_rho_template(), StiffenedGasFluidProperties::e_from_p_T(), LeadBismuthFluidProperties::e_from_p_T(), LeadFluidProperties::e_from_p_T(), CaloricallyImperfectGas::e_from_p_T(), IdealGasFluidProperties::e_from_p_T(), Water97FluidProperties::e_from_v_h(), TabulatedFluidProperties::e_from_v_h(), SimpleFluidProperties::e_from_v_h(), StiffenedGasFluidProperties::g_from_v_e(), IdealGasFluidProperties::g_from_v_e(), CaloricallyImperfectGas::g_from_v_e(), TabulatedFluidProperties::g_from_v_e(), CaloricallyImperfectGas::gamma_from_p_T(), TabulatedFluidProperties::generateTabulatedData(), LinearFluidProperties::h_from_p_T(), StiffenedGasFluidProperties::h_from_p_T(), LeadBismuthFluidProperties::h_from_p_T(), LeadFluidProperties::h_from_p_T(), CaloricallyImperfectGas::h_from_p_T(), IdealGasFluidProperties::h_from_p_T(), Water97FluidProperties::henryConstant(), LeadBismuthFluidProperties::k_from_p_T(), LeadFluidProperties::k_from_p_T(), CaloricallyImperfectGas::k_from_p_T(), IdealGasFluidProperties::k_from_p_T(), CaloricallyImperfectGas::k_from_v_e(), TabulatedFluidProperties::k_from_v_e(), Water97FluidProperties::k_from_v_e_template(), LeadBismuthFluidProperties::mu_from_p_T(), LeadFluidProperties::mu_from_p_T(), CaloricallyImperfectGas::mu_from_v_e(), TabulatedFluidProperties::mu_from_v_e(), StiffenedGasFluidProperties::p_from_h_s(), IdealGasFluidProperties::p_from_h_s(), CaloricallyImperfectGas::p_from_h_s(), StiffenedGasFluidProperties::p_from_T_v(), CaloricallyImperfectGas::p_from_T_v(), IdealGasFluidProperties::p_from_T_v(), LinearFluidProperties::p_from_v_e(), LeadBismuthFluidProperties::p_from_v_e(), LeadFluidProperties::p_from_v_e(), IdealGasFluidProperties::p_from_v_e(), LinearTestFluidProperties::p_from_v_e(), CaloricallyImperfectGas::p_from_v_e(), FlibeFluidProperties::p_from_v_e(), FlinakFluidProperties::p_from_v_e(), HeliumFluidProperties::p_from_v_e(), TemperaturePressureFunctionFluidProperties::p_from_v_e(), TabulatedFluidProperties::p_from_v_e(), SimpleFluidProperties::p_from_v_e(), Water97FluidProperties::p_from_v_e_template(), SimpleFluidProperties::p_from_v_h(), SinglePhaseFluidProperties::p_T_from_v_e(), Water97FluidProperties::p_T_from_v_e(), SinglePhaseFluidProperties::rho_e_from_p_T(), StiffenedGasFluidProperties::rho_from_p_s(), TabulatedFluidProperties::rho_from_p_s(), CaloricallyImperfectGas::rho_from_p_s(), IdealGasFluidProperties::rho_from_p_s(), TestSinglePhaseFluidProperties::rho_from_p_T(), LinearTestFluidProperties::rho_from_p_T(), TabulatedFluidProperties::rho_from_p_T(), LinearFluidProperties::rho_from_p_T(), CaloricallyImperfectGas::rho_from_p_T(), LeadBismuthFluidProperties::rho_from_p_T(), LeadFluidProperties::rho_from_p_T(), IdealGasFluidProperties::rho_from_p_T(), SinglePhaseFluidProperties::rho_mu_from_p_T(), Water97FluidProperties::rho_T_from_v_e(), StiffenedGasFluidProperties::s_from_h_p(), CaloricallyImperfectGas::s_from_h_p(), IdealGasFluidProperties::s_from_h_p(), CaloricallyImperfectGas::s_from_p_T(), IdealGasFluidProperties::s_from_p_T(), TabulatedFluidProperties::s_from_p_T(), CaloricallyImperfectGas::s_from_T_v(), IdealGasFluidProperties::s_from_T_v(), IdealGasFluidProperties::s_from_v_e(), Water97FluidProperties::T_drhodT_from_p_rho(), TabulatedFluidProperties::T_from_h_s(), LeadBismuthFluidProperties::T_from_p_h(), LeadFluidProperties::T_from_p_h(), TemperaturePressureFunctionFluidProperties::T_from_p_h(), CaloricallyImperfectGas::T_from_p_h(), SimpleFluidProperties::T_from_p_h(), Water97FluidProperties::T_from_p_h(), NaKFluidProperties::T_from_p_rho(), LeadBismuthFluidProperties::T_from_p_rho(), LeadFluidProperties::T_from_p_rho(), TemperaturePressureFunctionFluidProperties::T_from_p_rho(), FlibeFluidProperties::T_from_p_rho(), TabulatedFluidProperties::T_from_p_rho(), FlinakFluidProperties::T_from_p_rho(), SimpleFluidProperties::T_from_p_rho(), TabulatedFluidProperties::T_from_p_s(), FlibeFluidProperties::T_from_v_e(), FlinakFluidProperties::T_from_v_e(), SinglePhaseFluidProperties::v_e_from_p_T(), LeadBismuthFluidProperties::v_from_p_T(), LeadFluidProperties::v_from_p_T(), Water97FluidProperties::vaporPressure(), SinglePhaseFluidProperties::vaporPressure(), Water97FluidProperties::vaporTemperature(), SinglePhaseFluidProperties::vaporTemperature(), and TabulatedFluidProperties::writeTabulatedData().

◆ p [2/9]

e e e e s SinglePhaseFluidProperties::p
inherited

Definition at line 187 of file SinglePhaseFluidProperties.h.

◆ p [3/9]

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

Definition at line 191 of file SinglePhaseFluidProperties.h.

◆ p [4/9]

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

Definition at line 193 of file SinglePhaseFluidProperties.h.

◆ p [5/9]

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

Definition at line 195 of file SinglePhaseFluidProperties.h.

◆ p [6/9]

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

Definition at line 197 of file SinglePhaseFluidProperties.h.

◆ p [7/9]

e e e e s T T T T T rho v v SinglePhaseFluidProperties::p
inherited

Definition at line 203 of file SinglePhaseFluidProperties.h.

◆ p [8/9]

e e e e s T T T T T rho v v T s SinglePhaseFluidProperties::p
inherited

Definition at line 207 of file SinglePhaseFluidProperties.h.

◆ p [9/9]

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

Definition at line 209 of file SinglePhaseFluidProperties.h.

◆ propfuncWithDefault

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

Definition at line 212 of file SinglePhaseFluidProperties.h.

◆ rho

e e e e s T SinglePhaseFluidProperties::rho
inherited

Definition at line 189 of file SinglePhaseFluidProperties.h.

Referenced by HeliumFluidProperties::beta_from_p_T(), TemperaturePressureFunctionFluidProperties::beta_from_p_T(), FlinakFluidProperties::beta_from_p_T(), StiffenedGasFluidProperties::c2_from_p_rho(), HeliumFluidProperties::c_from_v_e(), TemperaturePressureFunctionFluidProperties::cp_from_p_T(), LeadFluidProperties::cv_from_p_T(), LeadBismuthFluidProperties::cv_from_p_T(), TestSinglePhaseFluidProperties::e_from_p_rho(), LinearTestFluidProperties::e_from_p_rho(), LinearFluidProperties::e_from_p_rho(), TabulatedFluidProperties::e_from_p_rho(), IdealGasFluidProperties::e_from_p_rho(), LeadBismuthFluidProperties::e_from_p_rho(), LeadFluidProperties::e_from_p_rho(), Water97FluidProperties::e_from_p_rho(), SimpleFluidProperties::e_from_p_rho(), TemperaturePressureFunctionFluidProperties::e_from_p_rho(), FlibeFluidProperties::e_from_p_rho(), FlinakFluidProperties::e_from_p_rho(), HeliumFluidProperties::e_from_p_rho(), Water97FluidProperties::e_from_p_rho_template(), NaKFluidProperties::e_from_p_T(), NaClFluidProperties::e_from_p_T(), LinearFluidProperties::h_from_p_T(), TemperaturePressureFunctionFluidProperties::h_from_p_T(), Water97FluidProperties::k_from_p_T_template(), CO2FluidProperties::mu_from_p_T(), NitrogenFluidProperties::mu_from_p_T(), NaKFluidProperties::mu_from_p_T(), HydrogenFluidProperties::mu_from_p_T(), Water97FluidProperties::mu_from_p_T(), Water97FluidProperties::mu_from_p_T_template(), Water97FluidProperties::mu_from_v_e(), Water97FluidProperties::p_from_v_e_template(), Water97FluidProperties::p_T_from_v_e(), SinglePhaseFluidProperties::rho_e_from_p_T(), StiffenedGasFluidProperties::rho_from_p_s(), TabulatedFluidProperties::rho_from_p_s(), IdealGasFluidProperties::rho_from_p_s(), TestSinglePhaseFluidProperties::rho_from_p_T(), LinearTestFluidProperties::rho_from_p_T(), SodiumSaturationFluidProperties::rho_from_p_T(), HelmholtzFluidProperties::rho_from_p_T(), TabulatedFluidProperties::rho_from_p_T(), NaKFluidProperties::rho_from_p_T(), LinearFluidProperties::rho_from_p_T(), CO2FluidProperties::rho_from_p_T(), NaClFluidProperties::rho_from_p_T(), LeadBismuthFluidProperties::rho_from_p_T(), CaloricallyImperfectGas::rho_from_p_T(), SalineMoltenSaltFluidProperties::rho_from_p_T(), LeadFluidProperties::rho_from_p_T(), IdealGasFluidProperties::rho_from_p_T(), Water97FluidProperties::rho_from_p_T(), SimpleFluidProperties::rho_from_p_T(), TemperaturePressureFunctionFluidProperties::rho_from_p_T(), FlibeFluidProperties::rho_from_p_T(), FlinakFluidProperties::rho_from_p_T(), HeliumFluidProperties::rho_from_p_T(), Water97FluidProperties::rho_from_p_T_template(), NitrogenFluidProperties::rho_mu_from_p_T(), HydrogenFluidProperties::rho_mu_from_p_T(), CO2FluidProperties::rho_mu_from_p_T(), Water97FluidProperties::rho_mu_from_p_T(), SinglePhaseFluidProperties::rho_mu_from_p_T(), Water97FluidProperties::rho_T_from_v_e(), Water97FluidProperties::T_drhodT_from_p_rho(), LeadBismuthFluidProperties::T_from_p_rho(), LeadFluidProperties::T_from_p_rho(), TemperaturePressureFunctionFluidProperties::T_from_p_rho(), FlibeFluidProperties::T_from_p_rho(), TabulatedFluidProperties::T_from_p_rho(), FlinakFluidProperties::T_from_p_rho(), SimpleFluidProperties::T_from_p_rho(), SinglePhaseFluidProperties::v_e_from_p_T(), TabulatedFluidProperties::v_from_p_T(), and TemperaturePressureFunctionFluidProperties::v_from_p_T().

◆ T [1/2]

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

Definition at line 199 of file SinglePhaseFluidProperties.h.

Referenced by LinearFluidProperties::beta_from_p_T(), LeadBismuthFluidProperties::bulk_modulus_from_p_T(), LeadFluidProperties::bulk_modulus_from_p_T(), CaloricallyImperfectGas::c_from_p_T(), IdealGasFluidProperties::c_from_p_T(), Water97FluidProperties::c_from_p_T(), Water97FluidProperties::c_from_p_T_template(), IdealGasFluidProperties::c_from_v_e(), LeadBismuthFluidProperties::c_from_v_e(), LeadFluidProperties::c_from_v_e(), CaloricallyImperfectGas::c_from_v_e(), HeliumFluidProperties::c_from_v_e(), TabulatedFluidProperties::c_from_v_e(), Water97FluidProperties::c_from_v_e(), SimpleFluidProperties::c_from_v_e(), TabulatedFluidProperties::checkInputVariables(), LeadBismuthFluidProperties::cp_from_p_T(), LeadFluidProperties::cp_from_p_T(), CaloricallyImperfectGas::cp_from_p_T(), IdealGasFluidProperties::cp_from_p_T(), TemperaturePressureFunctionFluidProperties::cp_from_p_T(), Water97FluidProperties::cp_from_p_T_template(), CaloricallyImperfectGas::cp_from_T(), CaloricallyImperfectGas::cp_from_v_e(), LeadBismuthFluidProperties::cp_from_v_e(), LeadFluidProperties::cp_from_v_e(), TemperaturePressureFunctionFluidProperties::cp_from_v_e(), TabulatedFluidProperties::cp_from_v_e(), Water97FluidProperties::cp_from_v_e(), LeadFluidProperties::cv_from_p_T(), LeadBismuthFluidProperties::cv_from_p_T(), CaloricallyImperfectGas::cv_from_p_T(), IdealGasFluidProperties::cv_from_p_T(), Water97FluidProperties::cv_from_p_T_template(), CaloricallyImperfectGas::cv_from_T(), CaloricallyImperfectGas::cv_from_T_v(), CaloricallyImperfectGas::cv_from_v_e(), LeadBismuthFluidProperties::cv_from_v_e(), LeadFluidProperties::cv_from_v_e(), TabulatedFluidProperties::cv_from_v_e(), Water97FluidProperties::cv_from_v_e(), Water97FluidProperties::d2gamma1_dpi2(), Water97FluidProperties::d2gamma1_dpitau(), Water97FluidProperties::d2gamma1_dtau2(), Water97FluidProperties::d2gamma2_dpi2(), Water97FluidProperties::d2gamma2_dpitau(), Water97FluidProperties::d2gamma2_dtau2(), Water97FluidProperties::d2gamma5_dpi2(), Water97FluidProperties::d2gamma5_dpitau(), Water97FluidProperties::d2gamma5_dtau2(), Water97FluidProperties::d2phi3_ddelta2(), Water97FluidProperties::d2phi3_ddeltatau(), Water97FluidProperties::d2phi3_dtau2(), Water97FluidProperties::densityRegion3(), Water97FluidProperties::dgamma1_dpi(), Water97FluidProperties::dgamma1_dtau(), Water97FluidProperties::dgamma2_dpi(), Water97FluidProperties::dgamma2_dtau(), Water97FluidProperties::dgamma5_dpi(), Water97FluidProperties::dgamma5_dtau(), Water97FluidProperties::dphi3_ddelta(), Water97FluidProperties::dphi3_dtau(), TabulatedFluidProperties::e_from_p_rho(), LeadBismuthFluidProperties::e_from_p_rho(), LeadFluidProperties::e_from_p_rho(), SimpleFluidProperties::e_from_p_rho(), StiffenedGasFluidProperties::e_from_p_T(), LeadBismuthFluidProperties::e_from_p_T(), CaloricallyImperfectGas::e_from_p_T(), LeadFluidProperties::e_from_p_T(), IdealGasFluidProperties::e_from_p_T(), Water97FluidProperties::e_from_p_T_template(), CaloricallyImperfectGas::e_from_T(), StiffenedGasFluidProperties::e_from_T_v(), CaloricallyImperfectGas::e_from_T_v(), IdealGasFluidProperties::e_from_T_v(), HeliumFluidProperties::e_from_T_v(), CaloricallyImperfectGas::e_from_v_h(), Water97FluidProperties::e_from_v_h(), TabulatedFluidProperties::e_from_v_h(), SimpleFluidProperties::e_from_v_h(), StiffenedGasFluidProperties::g_from_v_e(), IdealGasFluidProperties::g_from_v_e(), CaloricallyImperfectGas::g_from_v_e(), TabulatedFluidProperties::g_from_v_e(), Water97FluidProperties::gamma1(), Water97FluidProperties::gamma2(), Water97FluidProperties::gamma5(), CaloricallyImperfectGas::gamma_from_p_T(), LinearFluidProperties::h_from_p_T(), StiffenedGasFluidProperties::h_from_p_T(), LeadBismuthFluidProperties::h_from_p_T(), LeadFluidProperties::h_from_p_T(), CaloricallyImperfectGas::h_from_p_T(), IdealGasFluidProperties::h_from_p_T(), Water97FluidProperties::h_from_p_T_template(), CaloricallyImperfectGas::h_from_T(), StiffenedGasFluidProperties::h_from_T_v(), CaloricallyImperfectGas::h_from_T_v(), IdealGasFluidProperties::h_from_T_v(), LeadBismuthFluidProperties::h_from_v_e(), LeadFluidProperties::h_from_v_e(), Water97FluidProperties::henryConstant(), LeadBismuthFluidProperties::k_from_p_T(), LeadFluidProperties::k_from_p_T(), CaloricallyImperfectGas::k_from_p_T(), IdealGasFluidProperties::k_from_p_T(), Water97FluidProperties::k_from_p_T_template(), Water97FluidProperties::k_from_rho_T_template(), CaloricallyImperfectGas::k_from_v_e(), LeadBismuthFluidProperties::k_from_v_e(), LeadFluidProperties::k_from_v_e(), TabulatedFluidProperties::k_from_v_e(), HeliumFluidProperties::k_from_v_e(), SinglePhaseFluidProperties::makeZeroAndOne(), CaloricallyImperfectGas::mu_from_p_T(), LeadBismuthFluidProperties::mu_from_p_T(), LeadFluidProperties::mu_from_p_T(), IdealGasFluidProperties::mu_from_p_T(), Water97FluidProperties::mu_from_p_T_template(), Water97FluidProperties::mu_from_rho_T_template(), CaloricallyImperfectGas::mu_from_v_e(), LeadBismuthFluidProperties::mu_from_v_e(), LeadFluidProperties::mu_from_v_e(), TabulatedFluidProperties::mu_from_v_e(), Water97FluidProperties::mu_from_v_e(), CaloricallyImperfectGas::p_from_h_s(), StiffenedGasFluidProperties::p_from_T_v(), CaloricallyImperfectGas::p_from_T_v(), IdealGasFluidProperties::p_from_T_v(), HeliumFluidProperties::p_from_T_v(), CaloricallyImperfectGas::p_from_v_e(), HeliumFluidProperties::p_from_v_e(), FlibeFluidProperties::p_from_v_e(), FlinakFluidProperties::p_from_v_e(), TemperaturePressureFunctionFluidProperties::p_from_v_e(), Water97FluidProperties::p_from_v_e_template(), SimpleFluidProperties::p_from_v_h(), SinglePhaseFluidProperties::p_T_from_h_s(), SinglePhaseFluidProperties::p_T_from_v_e(), SinglePhaseFluidProperties::p_T_from_v_h(), Water97FluidProperties::p_T_from_v_h(), Water97FluidProperties::phi3(), SinglePhaseFluidProperties::rho_e_from_p_T(), StiffenedGasFluidProperties::rho_from_p_s(), TabulatedFluidProperties::rho_from_p_s(), CaloricallyImperfectGas::rho_from_p_s(), IdealGasFluidProperties::rho_from_p_s(), TestSinglePhaseFluidProperties::rho_from_p_T(), LinearTestFluidProperties::rho_from_p_T(), TabulatedFluidProperties::rho_from_p_T(), LinearFluidProperties::rho_from_p_T(), CaloricallyImperfectGas::rho_from_p_T(), LeadBismuthFluidProperties::rho_from_p_T(), LeadFluidProperties::rho_from_p_T(), IdealGasFluidProperties::rho_from_p_T(), Water97FluidProperties::rho_from_p_T_template(), SinglePhaseFluidProperties::rho_mu_from_p_T(), CaloricallyImperfectGas::s_from_h_p(), TabulatedFluidProperties::s_from_h_p(), CaloricallyImperfectGas::s_from_p_T(), IdealGasFluidProperties::s_from_p_T(), TabulatedFluidProperties::s_from_p_T(), StiffenedGasFluidProperties::s_from_T_v(), CaloricallyImperfectGas::s_from_T_v(), IdealGasFluidProperties::s_from_T_v(), CaloricallyImperfectGas::s_from_v_e(), IdealGasFluidProperties::s_from_v_e(), Water97FluidProperties::subregionVolume(), Water97FluidProperties::T_drhodT_from_p_rho(), TabulatedFluidProperties::T_from_h_p(), TabulatedFluidProperties::T_from_h_s(), LeadBismuthFluidProperties::T_from_p_h(), LeadFluidProperties::T_from_p_h(), TemperaturePressureFunctionFluidProperties::T_from_p_h(), CaloricallyImperfectGas::T_from_p_h(), IdealGasFluidProperties::T_from_p_h(), Water97FluidProperties::T_from_p_h(), NaKFluidProperties::T_from_p_rho(), LeadBismuthFluidProperties::T_from_p_rho(), LeadFluidProperties::T_from_p_rho(), TemperaturePressureFunctionFluidProperties::T_from_p_rho(), TabulatedFluidProperties::T_from_p_rho(), SimpleFluidProperties::T_from_p_rho(), TabulatedFluidProperties::T_from_p_s(), LinearFluidProperties::T_from_v_e(), LeadBismuthFluidProperties::T_from_v_e(), LinearTestFluidProperties::T_from_v_e(), LeadFluidProperties::T_from_v_e(), IdealGasFluidProperties::T_from_v_e(), CaloricallyImperfectGas::T_from_v_e(), FlibeFluidProperties::T_from_v_e(), FlinakFluidProperties::T_from_v_e(), HeliumFluidProperties::T_from_v_e(), SimpleFluidProperties::T_from_v_e(), TabulatedFluidProperties::T_from_v_e(), SimpleFluidProperties::T_from_v_h(), Water97FluidProperties::tempXY(), SinglePhaseFluidProperties::v_e_from_p_T(), LeadBismuthFluidProperties::v_from_p_T(), LeadFluidProperties::v_from_p_T(), SinglePhaseFluidProperties::vaporPressure(), Water97FluidProperties::vaporPressureTemplate(), Water97FluidProperties::vaporTemperature(), SinglePhaseFluidProperties::vaporTemperature(), and CaloricallyImperfectGas::Z_from_T().

◆ T [2/2]

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

Definition at line 201 of file SinglePhaseFluidProperties.h.

◆ v [1/5]

SinglePhaseFluidProperties::v
inherited

Definition at line 177 of file SinglePhaseFluidProperties.h.

Referenced by StiffenedGasFluidProperties::c_from_v_e(), LinearFluidProperties::c_from_v_e(), TestSinglePhaseFluidProperties::c_from_v_e(), IdealGasFluidProperties::c_from_v_e(), LeadBismuthFluidProperties::c_from_v_e(), LeadFluidProperties::c_from_v_e(), CaloricallyImperfectGas::c_from_v_e(), HeliumFluidProperties::c_from_v_e(), TabulatedFluidProperties::c_from_v_e(), Water97FluidProperties::c_from_v_e(), SimpleFluidProperties::c_from_v_e(), LinearFluidProperties::cp_from_v_e(), StiffenedGasFluidProperties::cp_from_v_e(), CaloricallyImperfectGas::cp_from_v_e(), TestSinglePhaseFluidProperties::cp_from_v_e(), LeadBismuthFluidProperties::cp_from_v_e(), IdealGasFluidProperties::cp_from_v_e(), LeadFluidProperties::cp_from_v_e(), SimpleFluidProperties::cp_from_v_e(), TemperaturePressureFunctionFluidProperties::cp_from_v_e(), FlibeFluidProperties::cp_from_v_e(), FlinakFluidProperties::cp_from_v_e(), TabulatedFluidProperties::cp_from_v_e(), HeliumFluidProperties::cp_from_v_e(), Water97FluidProperties::cp_from_v_e(), FlibeFluidProperties::cv_from_p_T(), FlinakFluidProperties::cv_from_p_T(), StiffenedGasFluidProperties::cv_from_v_e(), TestSinglePhaseFluidProperties::cv_from_v_e(), CaloricallyImperfectGas::cv_from_v_e(), IdealGasFluidProperties::cv_from_v_e(), LeadBismuthFluidProperties::cv_from_v_e(), LeadFluidProperties::cv_from_v_e(), SimpleFluidProperties::cv_from_v_e(), TemperaturePressureFunctionFluidProperties::cv_from_v_e(), FlibeFluidProperties::cv_from_v_e(), TabulatedFluidProperties::cv_from_v_e(), FlinakFluidProperties::cv_from_v_e(), Water97FluidProperties::cv_from_v_e(), HeliumFluidProperties::cv_from_v_e(), HeliumFluidProperties::e_from_p_rho(), SodiumSaturationFluidProperties::e_from_p_T(), LeadBismuthFluidProperties::e_from_p_T(), LeadFluidProperties::e_from_p_T(), FlibeFluidProperties::e_from_p_T(), FlinakFluidProperties::e_from_p_T(), StiffenedGasFluidProperties::e_from_T_v(), CaloricallyImperfectGas::e_from_T_v(), HeliumFluidProperties::e_from_T_v(), CaloricallyImperfectGas::e_from_v_h(), StiffenedGasFluidProperties::e_from_v_h(), IdealGasFluidProperties::e_from_v_h(), Water97FluidProperties::e_from_v_h(), TabulatedFluidProperties::e_from_v_h(), SimpleFluidProperties::e_from_v_h(), StiffenedGasFluidProperties::g_from_v_e(), IdealGasFluidProperties::g_from_v_e(), CaloricallyImperfectGas::g_from_v_e(), TabulatedFluidProperties::g_from_v_e(), CaloricallyImperfectGas::gamma_from_v_e(), LeadBismuthFluidProperties::h_from_v_e(), LeadFluidProperties::h_from_v_e(), StiffenedGasFluidProperties::k_from_v_e(), CaloricallyImperfectGas::k_from_v_e(), TestSinglePhaseFluidProperties::k_from_v_e(), LeadBismuthFluidProperties::k_from_v_e(), LeadFluidProperties::k_from_v_e(), TemperaturePressureFunctionFluidProperties::k_from_v_e(), TabulatedFluidProperties::k_from_v_e(), FlibeFluidProperties::k_from_v_e(), FlinakFluidProperties::k_from_v_e(), HeliumFluidProperties::k_from_v_e(), Water97FluidProperties::k_from_v_e(), Water97FluidProperties::k_from_v_e_template(), LinearTestFluidProperties::mu_from_v_e(), TestSinglePhaseFluidProperties::mu_from_v_e(), CaloricallyImperfectGas::mu_from_v_e(), LeadBismuthFluidProperties::mu_from_v_e(), LeadFluidProperties::mu_from_v_e(), TemperaturePressureFunctionFluidProperties::mu_from_v_e(), TabulatedFluidProperties::mu_from_v_e(), FlibeFluidProperties::mu_from_v_e(), FlinakFluidProperties::mu_from_v_e(), Water97FluidProperties::mu_from_v_e(), HeliumFluidProperties::mu_from_v_e(), CaloricallyImperfectGas::p_from_h_s(), StiffenedGasFluidProperties::p_from_T_v(), CaloricallyImperfectGas::p_from_T_v(), IdealGasFluidProperties::p_from_T_v(), HeliumFluidProperties::p_from_T_v(), TestConservedVarFluidProperties::p_from_v_e(), LinearFluidProperties::p_from_v_e(), LeadBismuthFluidProperties::p_from_v_e(), LeadFluidProperties::p_from_v_e(), IdealGasFluidProperties::p_from_v_e(), LinearTestFluidProperties::p_from_v_e(), CaloricallyImperfectGas::p_from_v_e(), HeliumFluidProperties::p_from_v_e(), FlibeFluidProperties::p_from_v_e(), FlinakFluidProperties::p_from_v_e(), SodiumSaturationFluidProperties::p_from_v_e(), TemperaturePressureFunctionFluidProperties::p_from_v_e(), Water97FluidProperties::p_from_v_e(), TabulatedFluidProperties::p_from_v_e(), SimpleFluidProperties::p_from_v_e(), Water97FluidProperties::p_from_v_e_template(), SimpleFluidProperties::p_from_v_h(), SinglePhaseFluidProperties::p_T_from_v_e(), Water97FluidProperties::p_T_from_v_e(), Water97FluidProperties::p_T_from_v_h(), SinglePhaseFluidProperties::p_T_from_v_h(), Water97FluidProperties::rho_T_from_v_e(), CaloricallyImperfectGas::s_from_h_p(), CaloricallyImperfectGas::s_from_p_T(), StiffenedGasFluidProperties::s_from_T_v(), CaloricallyImperfectGas::s_from_T_v(), IdealGasFluidProperties::s_from_T_v(), TestSinglePhaseFluidProperties::s_from_v_e(), CaloricallyImperfectGas::s_from_v_e(), IdealGasFluidProperties::s_from_v_e(), LinearFluidProperties::T_from_v_e(), LeadBismuthFluidProperties::T_from_v_e(), LinearTestFluidProperties::T_from_v_e(), LeadFluidProperties::T_from_v_e(), CaloricallyImperfectGas::T_from_v_e(), IdealGasFluidProperties::T_from_v_e(), SodiumSaturationFluidProperties::T_from_v_e(), FlibeFluidProperties::T_from_v_e(), FlinakFluidProperties::T_from_v_e(), HeliumFluidProperties::T_from_v_e(), SimpleFluidProperties::T_from_v_e(), TabulatedFluidProperties::T_from_v_e(), Water97FluidProperties::T_from_v_e(), SimpleFluidProperties::T_from_v_h(), SinglePhaseFluidProperties::v_e_from_p_T(), StiffenedGasFluidProperties::v_e_spndl_from_T(), CaloricallyImperfectGas::v_e_spndl_from_T(), IdealGasFluidProperties::v_e_spndl_from_T(), SodiumSaturationFluidProperties::v_from_p_T(), TabulatedFluidProperties::v_from_p_T(), Water97FluidProperties::v_from_p_T(), LeadBismuthFluidProperties::v_from_p_T(), LeadFluidProperties::v_from_p_T(), TemperaturePressureFunctionFluidProperties::v_from_p_T(), FlibeFluidProperties::v_from_p_T(), FlinakFluidProperties::v_from_p_T(), and Water97FluidProperties::v_from_p_T_template().

◆ v [2/5]

e SinglePhaseFluidProperties::v
inherited

Definition at line 179 of file SinglePhaseFluidProperties.h.

◆ v [3/5]

e e SinglePhaseFluidProperties::v
inherited

Definition at line 181 of file SinglePhaseFluidProperties.h.

◆ v [4/5]

e e e SinglePhaseFluidProperties::v
inherited

Definition at line 183 of file SinglePhaseFluidProperties.h.

◆ v [5/5]

e e e e s T T T T T rho v v T s h T SinglePhaseFluidProperties::v
inherited

Definition at line 211 of file SinglePhaseFluidProperties.h.


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