Base class equation of state for fluids that use a Helmholtz free energy alpha(delta, tau), where delta is a scaled density and tau is a scaled temperature. More...

#include <HelmholtzFluidProperties.h>

Inheritance diagram for HelmholtzFluidProperties:

[legend]

Public Types
typedef DataFileName	DataFileParameterType

Public Member Functions
	HelmholtzFluidProperties (const InputParameters &parameters)

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 virtual std Real	molarMass () const
	Fluid name. More...

virtual Real	criticalPressure () const
	Critical pressure. More...

virtual Real	criticalTemperature () const
	Critical temperature. More...

virtual Real	criticalDensity () const
	Critical density. More...

virtual Real	criticalInternalEnergy () const
	Critical specific internal energy. More...

virtual Real	triplePointPressure () const
	Triple point pressure. More...

virtual Real	triplePointTemperature () const
	Triple point temperature. More...

virtual Real	e_spndl_from_v (Real v) const
	Specific internal energy from temperature and specific volume. More...

virtual void	v_e_spndl_from_T (Real T, Real &v, Real &e) const
	Specific internal energy from temperature and specific volume. More...

virtual Real	vaporPressure (Real T) const
	Vapor pressure. More...

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

DualReal	vaporPressure (const DualReal &T) const

virtual Real	vaporTemperature (Real p) const
	Vapor temperature. More...

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

DualReal	vaporTemperature (const DualReal &p) const

virtual std::vector< Real >	henryCoefficients () const
	Henry's law coefficients for dissolution in water. More...

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, Real >	makeZeroAndOne (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

SubProblem &	getSubProblem () 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)

UserObject *	primaryThreadCopy ()

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

std::shared_ptr< MooseObject >	getSharedPtr ()

std::shared_ptr< const MooseObject >	getSharedPtr () const

MooseApp &	getMooseApp () 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 InputParameters &	parameters () const

MooseObjectName	uniqueName () const

const T &	getParam (const std::string &name) const

std::vector< std::pair< T1, T2 > >	getParam (const std::string &param1, const std::string &param2) const

const T &	getRenamedParam (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 ExecFlagEnum &	getExecuteOnEnum () const

UserObjectName	getUserObjectName (const std::string &param_name) const

const T &	getUserObject (const std::string &param_name, bool is_dependency=true) const

const T &	getUserObjectByName (const UserObjectName &object_name, bool is_dependency=true) const

const UserObject &	getUserObjectBase (const std::string &param_name, bool is_dependency=true) const

const UserObject &	getUserObjectBaseByName (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< SubdomainID >	getMaterialPropertyBlocks (const std::string &name)

std::vector< SubdomainName >	getMaterialPropertyBlockNames (const std::string &name)

std::set< BoundaryID >	getMaterialPropertyBoundaryIDs (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)

MaterialBase &	getMaterial (const std::string &name)

MaterialBase &	getMaterial (const std::string &name)

MaterialBase &	getMaterialByName (const std::string &name, bool no_warn=false)

MaterialBase &	getMaterialByName (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 Function &	getFunction (const std::string &name) const

const Function &	getFunctionByName (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 VectorPostprocessorValue &	getVectorPostprocessorValue (const std::string &param_name, const std::string &vector_name) const

const VectorPostprocessorValue &	getVectorPostprocessorValue (const std::string &param_name, const std::string &vector_name, bool needs_broadcast) const

const VectorPostprocessorValue &	getVectorPostprocessorValueByName (const VectorPostprocessorName &name, const std::string &vector_name) const

const VectorPostprocessorValue &	getVectorPostprocessorValueByName (const VectorPostprocessorName &name, const std::string &vector_name, bool needs_broadcast) const

const VectorPostprocessorValue &	getVectorPostprocessorValueOld (const std::string &param_name, const std::string &vector_name) const

const VectorPostprocessorValue &	getVectorPostprocessorValueOld (const std::string &param_name, const std::string &vector_name, bool needs_broadcast) const

const VectorPostprocessorValue &	getVectorPostprocessorValueOldByName (const VectorPostprocessorName &name, const std::string &vector_name) const

const VectorPostprocessorValue &	getVectorPostprocessorValueOldByName (const VectorPostprocessorName &name, const std::string &vector_name, bool needs_broadcast) const

const ScatterVectorPostprocessorValue &	getScatterVectorPostprocessorValue (const std::string &param_name, const std::string &vector_name) const

const ScatterVectorPostprocessorValue &	getScatterVectorPostprocessorValueByName (const VectorPostprocessorName &name, const std::string &vector_name) const

const ScatterVectorPostprocessorValue &	getScatterVectorPostprocessorValueOld (const std::string &param_name, const std::string &vector_name) const

const ScatterVectorPostprocessorValue &	getScatterVectorPostprocessorValueOldByName (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

T &	getSampler (const std::string &name)

Sampler &	getSampler (const std::string &name)

T &	getSamplerByName (const SamplerName &name)

Sampler &	getSamplerByName (const SamplerName &name)

virtual void	meshChanged ()

const std::vector< MooseVariableScalar *> &	getCoupledMooseScalarVars ()

const std::set< TagID > &	getScalarVariableCoupleableVectorTags () const

const std::set< TagID > &	getScalarVariableCoupleableMatrixTags () const

PerfGraph &	perfGraph ()

const PostprocessorValue &	getPostprocessorValue (const std::string &param_name, const unsigned int index=0) const

const PostprocessorValue &	getPostprocessorValue (const std::string &param_name, const unsigned int index=0) const

const PostprocessorValue &	getPostprocessorValueOld (const std::string &param_name, const unsigned int index=0) const

const PostprocessorValue &	getPostprocessorValueOld (const std::string &param_name, const unsigned int index=0) const

const PostprocessorValue &	getPostprocessorValueOlder (const std::string &param_name, const unsigned int index=0) const

const PostprocessorValue &	getPostprocessorValueOlder (const std::string &param_name, const unsigned int index=0) const

virtual const PostprocessorValue &	getPostprocessorValueByName (const PostprocessorName &name) const

virtual const PostprocessorValue &	getPostprocessorValueByName (const PostprocessorName &name) const

const PostprocessorValue &	getPostprocessorValueOldByName (const PostprocessorName &name) const

const PostprocessorValue &	getPostprocessorValueOldByName (const PostprocessorName &name) const

const PostprocessorValue &	getPostprocessorValueOlderByName (const PostprocessorName &name) const

const PostprocessorValue &	getPostprocessorValueOlderByName (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 Distribution &	getDistribution (const std::string &name) const

const T &	getDistribution (const std::string &name) const

const Distribution &	getDistribution (const std::string &name) const

const T &	getDistribution (const std::string &name) const

const Distribution &	getDistributionByName (const DistributionName &name) const

const T &	getDistributionByName (const std::string &name) const

const Distribution &	getDistributionByName (const DistributionName &name) const

const T &	getDistributionByName (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 =0
	Helmholtz free energy. More...

virtual Real	dalpha_ddelta (Real delta, Real tau) const =0
	Derivative of Helmholtz free energy wrt delta. More...

virtual Real	dalpha_dtau (Real delta, Real tau) const =0
	Derivative of Helmholtz free energy wrt tau. More...

virtual Real	d2alpha_ddelta2 (Real delta, Real tau) const =0
	Second derivative of Helmholtz free energy wrt delta. More...

virtual Real	d2alpha_dtau2 (Real delta, Real tau) const =0
	Second derivative of Helmholtz free energy wrt tau. More...

virtual Real	d2alpha_ddeltatau (Real delta, Real tau) const =0
	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 ReporterName &	getReporterName (const std::string &param_name) const

T &	declareRestartableData (const std::string &data_name, Args &&... args)

ManagedValue< T >	declareManagedRestartableDataWithContext (const std::string &data_name, void *context, Args &&... args)

const T &	getRestartableData (const std::string &data_name) const

T &	declareRestartableDataWithContext (const std::string &data_name, void *context, Args &&... args)

T &	declareRecoverableData (const std::string &data_name, Args &&... args)

T &	declareRestartableDataWithObjectName (const std::string &data_name, const std::string &object_name, Args &&... args)

T &	declareRestartableDataWithObjectNameWithContext (const std::string &data_name, const std::string &object_name, void *context, Args &&... args)

std::string	restartableName (const std::string &data_name) const

const T &	getMeshProperty (const std::string &data_name, const std::string &prefix)

const T &	getMeshProperty (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 VariableValue &	coupledScalarValue (const std::string &var_name, unsigned int comp=0) const

const ADVariableValue &	adCoupledScalarValue (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 VariableValue &	coupledVectorTagScalarValue (const std::string &var_name, TagID tag, unsigned int comp=0) const

const VariableValue &	coupledMatrixTagScalarValue (const std::string &var_name, TagID tag, unsigned int comp=0) const

const VariableValue &	coupledScalarValueOld (const std::string &var_name, unsigned int comp=0) const

const VariableValue &	coupledScalarValueOlder (const std::string &var_name, unsigned int comp=0) const

const VariableValue &	coupledScalarDot (const std::string &var_name, unsigned int comp=0) const

const ADVariableValue &	adCoupledScalarDot (const std::string &var_name, unsigned int comp=0) const

const VariableValue &	coupledScalarDotDot (const std::string &var_name, unsigned int comp=0) const

const VariableValue &	coupledScalarDotOld (const std::string &var_name, unsigned int comp=0) const

const VariableValue &	coupledScalarDotDotOld (const std::string &var_name, unsigned int comp=0) const

const VariableValue &	coupledScalarDotDu (const std::string &var_name, unsigned int comp=0) const

const VariableValue &	coupledScalarDotDotDu (const std::string &var_name, unsigned int comp=0) const

const MooseVariableScalar *	getScalarVar (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 T &	getReporterValue (const std::string &param_name, const std::size_t time_index=0)

const T &	getReporterValue (const std::string &param_name, ReporterMode mode, const std::size_t time_index=0)

const T &	getReporterValue (const std::string &param_name, const std::size_t time_index=0)

const T &	getReporterValue (const std::string &param_name, ReporterMode mode, const std::size_t time_index=0)

const T &	getReporterValueByName (const ReporterName &reporter_name, const std::size_t time_index=0)

const T &	getReporterValueByName (const ReporterName &reporter_name, ReporterMode mode, const std::size_t time_index=0)

const T &	getReporterValueByName (const ReporterName &reporter_name, const std::size_t time_index=0)

const T &	getReporterValueByName (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, T >	makeZeroAndOne (const T &)
	Given a type example, this method returns zero and unity representations 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	_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...

e	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 T s	propfunc (T, h, p) propfuncWithDefault(T

	v

e	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 T s	p

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 T e	propfuncWithDefault (gamma, p, T)

Detailed Description

Base class equation of state for fluids that use a Helmholtz free energy alpha(delta, tau), where delta is a scaled density and tau is a scaled temperature.

To implement a fluid using the Helmholtz EOS, inherit from this base class and override the method alpha(delta, tau) and its first and second derivatives wrt delta and tau. Thermophysical properties such as enthalpy, internal energy etc, will be calculated from the Helmholtz free energy.

Transport properties such as viscosity and thermal conductivity will need to be implemented in any derived class as required.

Definition at line 29 of file HelmholtzFluidProperties.h.

Constructor & Destructor Documentation

◆ HelmholtzFluidProperties()

HelmholtzFluidProperties::HelmholtzFluidProperties ( const InputParameters & parameters )

Definition at line 22 of file HelmholtzFluidProperties.C.

   : SinglePhaseFluidProperties(parameters)
 {
 }

Member Function Documentation

◆ alpha()

virtual Real HelmholtzFluidProperties::alpha	(	Real	delta,
		Real	tau
	)		const

protectedpure virtual

Helmholtz free energy.

Parameters

delta	scaled density (-)
tau	scaled temperature (-)

Returns: alpha Helmholtz free energy

Implemented in CO2FluidProperties, NitrogenFluidProperties, HydrogenFluidProperties, and MethaneFluidProperties.

Referenced by s_from_p_T().

◆ c_from_p_T()

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

overridevirtual

Definition at line 98 of file HelmholtzFluidProperties.C.

 {
   // Require density first
   const Real density = rho_from_p_T(pressure, temperature);
   // Scale the input density and temperature
   const Real delta = density / criticalDensity();
   const Real tau = criticalTemperature() / temperature;
 
   const Real da_dd = dalpha_ddelta(delta, tau);
 
   Real w = 2.0 * delta * da_dd + delta * delta * d2alpha_ddelta2(delta, tau);
   w -= Utility::pow<2>(delta * da_dd - delta * tau * d2alpha_ddeltatau(delta, tau)) /
        (tau * tau * d2alpha_dtau2(delta, tau));
 
   return std::sqrt(_R * temperature * w / molarMass());
 }

◆ cp_from_p_T()

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

overridevirtual

Definition at line 116 of file HelmholtzFluidProperties.C.

 {
   // Require density first
   const Real density = rho_from_p_T(pressure, temperature);
   // Scale the input density and temperature
   const Real delta = density / criticalDensity();
   const Real tau = criticalTemperature() / temperature;
 
   const Real da_dd = dalpha_ddelta(delta, tau);
 
   const Real cp = _R *
                   (-tau * tau * d2alpha_dtau2(delta, tau) +
                    Utility::pow<2>(delta * da_dd - delta * tau * d2alpha_ddeltatau(delta, tau)) /
                        (2.0 * delta * da_dd + delta * delta * d2alpha_ddelta2(delta, tau))) /
                   molarMass();
 
   return cp;
 }

◆ criticalDensity()

Real SinglePhaseFluidProperties::criticalDensity ( ) const

virtualinherited

Critical density.

Returns: critical density (kg/m^3)

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

Definition at line 291 of file SinglePhaseFluidProperties.C.

Referenced by c_from_p_T(), cp_from_p_T(), cv_from_p_T(), e_from_p_T(), h_from_p_T(), p_from_rho_T(), IdealRealGasMixtureFluidProperties::p_T_from_v_e(), rho_from_p_T(), s_from_p_T(), IdealRealGasMixtureFluidProperties::T_from_p_v(), and IdealRealGasMixtureFluidProperties::v_from_p_T().

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

◆ 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().

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

◆ criticalPressure()

Real SinglePhaseFluidProperties::criticalPressure ( ) const

virtualinherited

Critical pressure.

Returns: critical pressure (Pa)

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

Definition at line 279 of file SinglePhaseFluidProperties.C.

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

◆ criticalTemperature()

Real SinglePhaseFluidProperties::criticalTemperature ( ) const

virtualinherited

Critical temperature.

Returns: critical temperature (K)

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

Definition at line 285 of file SinglePhaseFluidProperties.C.

Referenced by c_from_p_T(), cp_from_p_T(), cv_from_p_T(), e_from_p_T(), h_from_p_T(), p_from_rho_T(), rho_from_p_T(), s_from_p_T(), IdealRealGasMixtureFluidProperties::v_from_p_T(), and IdealRealGasMixtureFluidProperties::xs_prim_from_p_T().

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

◆ cv_from_p_T()

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

overridevirtual

Definition at line 136 of file HelmholtzFluidProperties.C.

 {
   // Require density first
   const Real density = rho_from_p_T(pressure, temperature);
   // Scale the input density and temperature
   const Real delta = density / criticalDensity();
   const Real tau = criticalTemperature() / temperature;
 
   return -_R * tau * tau * d2alpha_dtau2(delta, tau) / molarMass();
 }

◆ d2alpha_ddelta2()

virtual Real HelmholtzFluidProperties::d2alpha_ddelta2	(	Real	delta,
		Real	tau
	)		const

protectedpure virtual

Second derivative of Helmholtz free energy wrt delta.

Parameters

delta	scaled density (-)
tau	scaled temperature (-)

Returns: second derivative of Helmholtz free energy wrt delta

Implemented in CO2FluidProperties, HydrogenFluidProperties, NitrogenFluidProperties, and MethaneFluidProperties.

Referenced by c_from_p_T(), cp_from_p_T(), e_from_p_T(), h_from_p_T(), rho_from_p_T(), and s_from_p_T().

◆ d2alpha_ddeltatau()

virtual Real HelmholtzFluidProperties::d2alpha_ddeltatau	(	Real	delta,
		Real	tau
	)		const

protectedpure virtual

Second derivative of Helmholtz free energy wrt delta and tau.

Parameters

delta	scaled density (-)
tau	scaled temperature (-)

Returns: second derivative of Helmholtz free energy wrt delta and tau

Implemented in CO2FluidProperties, HydrogenFluidProperties, NitrogenFluidProperties, and MethaneFluidProperties.

Referenced by c_from_p_T(), cp_from_p_T(), e_from_p_T(), h_from_p_T(), rho_from_p_T(), and s_from_p_T().

◆ d2alpha_dtau2()

virtual Real HelmholtzFluidProperties::d2alpha_dtau2	(	Real	delta,
		Real	tau
	)		const

protectedpure virtual

Second derivative of Helmholtz free energy wrt tau.

Parameters

delta	scaled density (-)
tau	scaled temperature (-)

Returns: second derivative of Helmholtz free energy wrt tau

Implemented in CO2FluidProperties, HydrogenFluidProperties, NitrogenFluidProperties, and MethaneFluidProperties.

Referenced by c_from_p_T(), cp_from_p_T(), cv_from_p_T(), e_from_p_T(), h_from_p_T(), and s_from_p_T().

◆ dalpha_ddelta()

virtual Real HelmholtzFluidProperties::dalpha_ddelta	(	Real	delta,
		Real	tau
	)		const

protectedpure virtual

Derivative of Helmholtz free energy wrt delta.

Parameters

delta	scaled density (-)
tau	scaled temperature (-)

Returns: derivative of Helmholtz free energy wrt delta

Implemented in CO2FluidProperties, NitrogenFluidProperties, HydrogenFluidProperties, and MethaneFluidProperties.

Referenced by c_from_p_T(), cp_from_p_T(), e_from_p_T(), h_from_p_T(), p_from_rho_T(), rho_from_p_T(), and s_from_p_T().

◆ dalpha_dtau()

virtual Real HelmholtzFluidProperties::dalpha_dtau	(	Real	delta,
		Real	tau
	)		const

protectedpure virtual

Derivative of Helmholtz free energy wrt tau.

Parameters

delta	scaled density (-)
tau	scaled temperature (-)

Returns: derivative of Helmholtz free energy wrt tau

Implemented in CO2FluidProperties, HydrogenFluidProperties, NitrogenFluidProperties, and MethaneFluidProperties.

Referenced by e_from_p_T(), h_from_p_T(), and s_from_p_T().

◆ e_from_p_T() [1/2]

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

overridevirtual

Definition at line 63 of file HelmholtzFluidProperties.C.

Referenced by e_from_p_T().

 {
   // Require density first
   const Real density = rho_from_p_T(pressure, temperature);
   // Scale the input density and temperature
   const Real delta = density / criticalDensity();
   const Real tau = criticalTemperature() / temperature;
 
   return _R * temperature * tau * dalpha_dtau(delta, tau) / molarMass();
 }

◆ 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

overridevirtual

Definition at line 75 of file HelmholtzFluidProperties.C.

 {
   e = this->e_from_p_T(pressure, temperature);
 
   // Require density first
   const Real density = rho_from_p_T(pressure, temperature);
   // Scale the input density and temperature
   const Real delta = density / criticalDensity();
   const Real tau = criticalTemperature() / temperature;
 
   const Real da_dd = dalpha_ddelta(delta, tau);
   const Real d2a_dd2 = d2alpha_ddelta2(delta, tau);
   const Real d2a_ddt = d2alpha_ddeltatau(delta, tau);
 
   de_dp = tau * d2a_ddt / (density * (2.0 * da_dd + delta * d2a_dd2));
   de_dT = -_R *
           (delta * tau * d2a_ddt * (da_dd - tau * d2a_ddt) / (2.0 * da_dd + delta * d2a_dd2) +
            tau * tau * d2alpha_dtau2(delta, tau)) /
           molarMass();
 }

◆ e_spndl_from_v()

Real SinglePhaseFluidProperties::e_spndl_from_v ( Real v ) const

virtualinherited

Specific internal energy from temperature and specific volume.

Parameters

[in]	T	temperature
[in]	v	specific volume

Reimplemented in IdealGasFluidProperties, 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().

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

◆ 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 {}

◆ h_from_p_T() [1/2]

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

overridevirtual

Definition at line 183 of file HelmholtzFluidProperties.C.

Referenced by h_from_p_T().

 {
   // Require density first
   const Real density = rho_from_p_T(pressure, temperature);
   // Scale the input density and temperature
   const Real delta = density / criticalDensity();
   const Real tau = criticalTemperature() / temperature;
 
   return _R * temperature * (tau * dalpha_dtau(delta, tau) + delta * dalpha_ddelta(delta, tau)) /
          molarMass();
 }

◆ 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

overridevirtual

Definition at line 196 of file HelmholtzFluidProperties.C.

 {
   h = this->h_from_p_T(pressure, temperature);
 
   // Require density first
   const Real density = rho_from_p_T(pressure, temperature);
   // Scale the input density and temperature
   const Real delta = density / criticalDensity();
   const Real tau = criticalTemperature() / temperature;
 
   const Real da_dd = dalpha_ddelta(delta, tau);
   const Real d2a_dd2 = d2alpha_ddelta2(delta, tau);
   const Real d2a_ddt = d2alpha_ddeltatau(delta, tau);
 
   dh_dp = (da_dd + delta * d2a_dd2 + tau * d2a_ddt) / (density * (2.0 * da_dd + delta * d2a_dd2));
   dh_dT = _R *
           (delta * da_dd * (1.0 - tau * d2a_ddt / da_dd) * (1.0 - tau * d2a_ddt / da_dd) /
                (2.0 + delta * d2a_dd2 / da_dd) -
            tau * tau * d2alpha_dtau2(delta, tau)) /
           molarMass();
 }

◆ henryCoefficients()

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

virtualinherited

Henry's law coefficients for dissolution in water.

Returns: Henry's constant coefficients

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

Definition at line 354 of file SinglePhaseFluidProperties.C.

Referenced by TabulatedFluidProperties::henryCoefficients().

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

◆ initialize()

virtual void FluidProperties::initialize ( )

inlinefinalvirtualinherited

Implements ThreadedGeneralUserObject.

Definition at line 34 of file FluidProperties.h.

34 {}

◆ 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 representations of that type (first and second members of returned pair respectively)

Definition at line 473 of file SinglePhaseFluidProperties.h.

Referenced by SinglePhaseFluidProperties::xyDerivatives().

 {
   return {T{0, 0}, T{1, 0}};
 }

◆ makeZeroAndOne() [2/2]

template<>

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

inlineinherited

Definition at line 480 of file SinglePhaseFluidProperties.h.

 {
   return {Real{0}, Real{1}};
 }

◆ molarMass()

Real SinglePhaseFluidProperties::molarMass ( ) const

virtualinherited

Fluid name.

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

Reimplemented in FlinakFluidProperties, FlibeFluidProperties, HeliumFluidProperties, IdealGasFluidProperties, CaloricallyImperfectGas, CO2FluidProperties, StiffenedGasFluidProperties, LinearFluidProperties, SodiumSaturationFluidProperties, NaClFluidProperties, Water97FluidProperties, HydrogenFluidProperties, MethaneFluidProperties, NitrogenFluidProperties, SimpleFluidProperties, TabulatedFluidProperties, NaKFluidProperties, LeadBismuthFluidProperties, and LeadFluidProperties.

Definition at line 267 of file SinglePhaseFluidProperties.C.

Referenced by BrineFluidProperties::BrineFluidProperties(), c_from_p_T(), cp_from_p_T(), cv_from_p_T(), e_from_p_T(), h_from_p_T(), IdealRealGasMixtureFluidProperties::k_from_p_T(), IdealRealGasMixtureFluidProperties::k_from_T_v(), TabulatedFluidProperties::molarMass(), IdealRealGasMixtureFluidProperties::mu_from_p_T(), IdealRealGasMixtureFluidProperties::mu_from_T_v(), p_from_rho_T(), rho_from_p_T(), s_from_p_T(), and IdealRealGasMixtureFluidProperties::v_from_p_T().

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

◆ p_from_rho_T()

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

virtual

Pressure as a function of density and temperature.

Parameters

rho	density (kg/m^3)
T	temperature (K)

Returns: pressure (Pa)

Reimplemented in CO2FluidProperties.

Definition at line 220 of file HelmholtzFluidProperties.C.

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

 {
   // Scale the input density and temperature
   const Real delta = density / criticalDensity();
   const Real tau = criticalTemperature() / temperature;
 
   return _R * density * temperature * delta * dalpha_ddelta(delta, tau) / molarMass();
 }

◆ 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]	h	specific enthalpy (J / kg)
[in]	s	specific entropy (J/K*kg)
[in]	p0	initial guess for pressure (Pa / kg)
[in]	T0	initial guess for temperature (K)
[out]	fluid	pressure (Pa / kg)
[out]	Temperature	(K)

Definition at line 572 of file SinglePhaseFluidProperties.h.

Referenced by TabulatedFluidProperties::T_from_h_s().

 {
   auto h_lambda = [&](const T & pressure, const T & temperature, T & new_h, T & dh_dp, T & dh_dT)
   { h_from_p_T(pressure, temperature, new_h, dh_dp, dh_dT); };
   auto s_lambda = [&](const T & pressure, const T & temperature, T & new_s, T & ds_dp, T & ds_dT)
   { s_from_p_T(pressure, temperature, new_s, ds_dp, ds_dT); };
   try
   {
     FluidPropertiesUtils::NewtonSolve2D(
         h, s, p0, T0, pressure, temperature, _tolerance, _tolerance, h_lambda, s_lambda);
     conversion_succeeded = true;
   }
   catch (MooseException &)
   {
     conversion_succeeded = false;
   }
 
   if (!conversion_succeeded)
     mooseDoOnce(mooseWarning("Conversion from (h, s)=(", h, ", ", s, ") to (p, T) failed"));
 }

◆ 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]	v	specific volume (m^3 / kg)
[in]	e	specific internal energy (J / kg)
[in]	p0	initial guess for pressure (Pa / kg)
[in]	T0	initial guess for temperature (K)
[out]	fluid	pressure (Pa / kg)
[out]	Temperature	(K)

Definition at line 508 of file SinglePhaseFluidProperties.h.

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

 {
   auto v_lambda = [&](const CppType & pressure,
                       const CppType & temperature,
                       CppType & new_v,
                       CppType & dv_dp,
                       CppType & dv_dT) { v_from_p_T(pressure, temperature, new_v, dv_dp, dv_dT); };
   auto e_lambda = [&](const CppType & pressure,
                       const CppType & temperature,
                       CppType & new_e,
                       CppType & de_dp,
                       CppType & de_dT) { e_from_p_T(pressure, temperature, new_e, de_dp, de_dT); };
   try
   {
     FluidPropertiesUtils::NewtonSolve2D(
         v, e, p0, T0, p, T, _tolerance, _tolerance, v_lambda, e_lambda);
     conversion_succeeded = true;
   }
   catch (MooseException &)
   {
     conversion_succeeded = false;
   }
 
   if (!conversion_succeeded)
     mooseDoOnce(mooseWarning("Conversion from (v, e)=(", v, ", ", e, ") to (p, T) failed"));
 }

◆ 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]	v	specific volume (m^3 / kg)
[in]	h	specific enthalpy (J / kg)
[in]	p0	initial guess for pressure (Pa / kg)
[in]	T0	initial guess for temperature (K)
[out]	fluid	pressure (Pa / kg)
[out]	Temperature	(K)

Definition at line 543 of file SinglePhaseFluidProperties.h.

Referenced by TabulatedBicubicFluidProperties::constructInterpolation().

 {
   auto v_lambda = [&](const T & pressure, const T & temperature, T & new_v, T & dv_dp, T & dv_dT)
   { v_from_p_T(pressure, temperature, new_v, dv_dp, dv_dT); };
   auto h_lambda = [&](const T & pressure, const T & temperature, T & new_h, T & dh_dp, T & dh_dT)
   { h_from_p_T(pressure, temperature, new_h, dh_dp, dh_dT); };
   try
   {
     FluidPropertiesUtils::NewtonSolve2D(
         v, h, p0, T0, pressure, temperature, _tolerance, _tolerance, v_lambda, h_lambda);
     conversion_succeeded = true;
   }
   catch (MooseException &)
   {
     conversion_succeeded = false;
   }
 
   if (!conversion_succeeded)
     mooseDoOnce(mooseWarning("Conversion from (v, h)=(", v, ", ", h, ") to (p, T) failed"));
 }

◆ propfunc() [1/14]

SinglePhaseFluidProperties::propfunc	(	p	,
		v	,
		e
	)

inherited

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

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

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

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

inherited

◆ propfunc() [3/14]

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

inherited

◆ propfunc() [4/14]

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

inherited

◆ propfunc() [5/14]

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

inherited

◆ propfunc() [6/14]

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

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	(	e	,
		p	,
		T
	)

inherited

◆ rho_e_from_p_T()

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

virtualinherited

Definition at line 413 of file SinglePhaseFluidProperties.C.

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

◆ rho_from_p_T() [1/2]

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

overridevirtual

Reimplemented in CO2FluidProperties.

Definition at line 28 of file HelmholtzFluidProperties.C.

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

 {
   Real density;
   // Initial estimate of a bracketing interval for the density
   Real lower_density = 1.0e-2;
   Real upper_density = 100.0;
 
   // The density is found by finding the zero of the pressure
   auto pressure_diff = [&pressure, &temperature, this](Real x)
   { return this->p_from_rho_T(x, temperature) - pressure; };
 
   BrentsMethod::bracket(pressure_diff, lower_density, upper_density);
   density = BrentsMethod::root(pressure_diff, lower_density, upper_density);
 
   return density;
 }

◆ 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

overridevirtual

Reimplemented in CO2FluidProperties.

Definition at line 46 of file HelmholtzFluidProperties.C.

 {
   rho = this->rho_from_p_T(pressure, temperature);
 
   // Scale the density and temperature
   const Real delta = rho / criticalDensity();
   const Real tau = criticalTemperature() / temperature;
   const Real da_dd = dalpha_ddelta(delta, tau);
   const Real d2a_dd2 = d2alpha_ddelta2(delta, tau);
 
   drho_dp = molarMass() / (_R * temperature * delta * (2.0 * da_dd + delta * d2a_dd2));
   drho_dT = rho * (tau * d2alpha_ddeltatau(delta, tau) - da_dd) / temperature /
             (2.0 * da_dd + delta * d2a_dd2);
 }

◆ 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().

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

◆ rho_mu_from_p_T() [2/3]

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

virtualinherited

Reimplemented in Water97FluidProperties, CO2FluidProperties, HydrogenFluidProperties, and NitrogenFluidProperties.

Definition at line 434 of file SinglePhaseFluidProperties.C.

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

◆ rho_mu_from_p_T() [3/3]

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

virtualinherited

Definition at line 448 of file SinglePhaseFluidProperties.C.

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

◆ s_from_p_T() [1/2]

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

overridevirtual

Definition at line 148 of file HelmholtzFluidProperties.C.

Referenced by s_from_p_T().

 {
   // Require density first
   const Real density = rho_from_p_T(pressure, temperature);
   // Scale the input density and temperature
   const Real delta = density / criticalDensity();
   const Real tau = criticalTemperature() / temperature;
 
   return _R * (tau * dalpha_dtau(delta, tau) - alpha(delta, tau)) / molarMass();
 }

◆ 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

overridevirtual

Definition at line 160 of file HelmholtzFluidProperties.C.

 {
   s = this->s_from_p_T(pressure, temperature);
 
   // Require density first
   const Real density = rho_from_p_T(pressure, temperature);
   // Scale the input density and temperature
   const Real delta = density / criticalDensity();
   const Real tau = criticalTemperature() / temperature;
 
   const Real da_dd = dalpha_ddelta(delta, tau);
   const Real da_dt = dalpha_dtau(delta, tau);
   const Real d2a_dd2 = d2alpha_ddelta2(delta, tau);
   const Real d2a_dt2 = d2alpha_dtau2(delta, tau);
   const Real d2a_ddt = d2alpha_ddeltatau(delta, tau);
 
   ds_dp = tau * (d2a_ddt - da_dd) / (density * temperature * (2.0 * da_dd + delta * d2a_dd2));
   ds_dT = -_R * tau * (da_dt - alpha(delta, tau) + tau * (d2a_dt2 - da_dt)) /
           (molarMass() * temperature);
 }

◆ 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 SinglePhaseFluidProperties::triplePointPressure ( ) const

virtualinherited

Triple point pressure.

Returns: triple point pressure (Pa)

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

Definition at line 303 of file SinglePhaseFluidProperties.C.

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

◆ triplePointTemperature()

Real SinglePhaseFluidProperties::triplePointTemperature ( ) const

virtualinherited

Triple point temperature.

Returns: triple point temperature (K)

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

Definition at line 309 of file SinglePhaseFluidProperties.C.

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

◆ 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 601 of file SinglePhaseFluidProperties.h.

 {
   const CppType rho = rho_from_p_T(p, T);
   v = 1.0 / rho;
   try
   {
     // more likely to not involve a Newton search
     e = e_from_p_T(p, T);
   }
   catch (...)
   {
     e = e_from_p_rho(p, rho);
   }
 }

◆ 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 621 of file SinglePhaseFluidProperties.h.

 {
   CppType rho, drho_dp, drho_dT;
   rho_from_p_T(p, T, rho, drho_dp, drho_dT);
 
   v = 1.0 / rho;
   const CppType dv_drho = -1.0 / (rho * rho);
   dv_dp = dv_drho * drho_dp;
   dv_dT = dv_drho * drho_dT;
 
   CppType de_dp_partial, de_drho;
   e_from_p_rho(p, rho, e, de_dp_partial, de_drho);
   de_dp = de_dp_partial + de_drho * drho_dp;
   de_dT = de_drho * drho_dT;
 }

◆ v_e_spndl_from_T()

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

virtualinherited

Specific internal energy from temperature and specific volume.

Parameters

[in]	T	temperature
[in]	v	specific volume

Reimplemented in IdealGasFluidProperties, CaloricallyImperfectGas, and StiffenedGasFluidProperties.

Definition at line 463 of file SinglePhaseFluidProperties.C.

Referenced by IdealRealGasMixtureFluidProperties::v_from_p_T().

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

◆ validParams()

InputParameters HelmholtzFluidProperties::validParams ( )

static

Definition at line 15 of file HelmholtzFluidProperties.C.

Referenced by MethaneFluidProperties::validParams(), NitrogenFluidProperties::validParams(), HydrogenFluidProperties::validParams(), and CO2FluidProperties::validParams().

 {
   InputParameters params = SinglePhaseFluidProperties::validParams();
   params.addClassDescription("Base class for Helmholtz free energy fluid EOS");
   return params;
 }

◆ vaporPressure() [1/3]

Real SinglePhaseFluidProperties::vaporPressure ( Real T ) const

virtualinherited

Vapor pressure.

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

Parameters

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

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

Definition at line 348 of file SinglePhaseFluidProperties.C.

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

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

◆ vaporPressure() [2/3]

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

virtualinherited

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

Definition at line 360 of file SinglePhaseFluidProperties.C.

 {
   unimplementedDerivativeMethod(__PRETTY_FUNCTION__);
 
   dp_dT = 0.0;
   p = vaporPressure(T);
 }

◆ vaporPressure() [3/3]

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

inherited

Definition at line 369 of file SinglePhaseFluidProperties.C.

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

◆ 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

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

Reimplemented in Water97FluidProperties.

Definition at line 383 of file SinglePhaseFluidProperties.C.

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

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

◆ 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.

 {
   unimplementedDerivativeMethod(__PRETTY_FUNCTION__);
 
   dT_dp = 0.0;
   T = vaporTemperature(p);
 }

◆ vaporTemperature() [3/3]

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

inherited

Definition at line 398 of file SinglePhaseFluidProperties.C.

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

◆ 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 487 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().

 {
   typedef MetaPhysicL::DualNumber<T, MetaPhysicL::NumberArray<2, T>> CompoundType;
   const auto [zero, one] = makeZeroAndOne(x);
 
   CompoundType x_c(x, zero);
   auto & x_cd = x_c.derivatives();
   x_cd[0] = one;
   CompoundType y_c(y, zero);
   auto & y_cd = y_c.derivatives();
   y_cd[1] = one;
 
   const auto z_c = z_from_x_y(x_c, y_c);
   z = z_c.value();
   dz_dx = z_c.derivatives()[0];
   dz_dy = z_c.derivatives()[1];
 }

Member Data Documentation

◆ _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::unimplementedDerivativeMethod().

◆ _p_initial_guess

const Real SinglePhaseFluidProperties::_p_initial_guess

protectedinherited

Definition at line 446 of file SinglePhaseFluidProperties.h.

Referenced by TabulatedFluidProperties::checkInitialGuess(), TabulatedBicubicFluidProperties::constructInterpolation(), TabulatedFluidProperties::g_from_v_e(), TemperaturePressureFunctionFluidProperties::p_from_v_e(), Water97FluidProperties::p_from_v_e_template(), Water97FluidProperties::p_T_from_v_h(), and TabulatedFluidProperties::T_from_h_s().

◆ _R

const Real FluidProperties::_R = 8.3144598

staticinherited

Universal gas constant (J/mol/K)

Definition at line 41 of file FluidProperties.h.

Referenced by c_from_p_T(), IdealGasFluidProperties::c_from_p_T(), cp_from_p_T(), cv_from_p_T(), e_from_p_T(), h_from_p_T(), p_from_rho_T(), rho_from_p_T(), CaloricallyImperfectGas::rho_from_p_T(), IdealGasFluidProperties::rho_from_p_T(), and s_from_p_T().

◆ _T_c2k

const Real FluidProperties::_T_c2k

protectedinherited

Conversion of temperature from Celsius to Kelvin.

Definition at line 45 of file FluidProperties.h.

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

◆ _T_initial_guess

const Real SinglePhaseFluidProperties::_T_initial_guess

protectedinherited

Definition at line 445 of file SinglePhaseFluidProperties.h.

◆ _tolerance

const Real SinglePhaseFluidProperties::_tolerance

protectedinherited

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.

Definition at line 444 of file SinglePhaseFluidProperties.h.

◆ h

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

inherited

Definition at line 210 of file SinglePhaseFluidProperties.h.

◆ p [1/9]

e e e e SinglePhaseFluidProperties::p

inherited

Definition at line 190 of file SinglePhaseFluidProperties.h.

◆ p [2/9]

e e e e s SinglePhaseFluidProperties::p

inherited

Definition at line 192 of file SinglePhaseFluidProperties.h.

◆ p [3/9]

e e e e s T T SinglePhaseFluidProperties::p

inherited

Definition at line 196 of file SinglePhaseFluidProperties.h.

◆ p [4/9]

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

inherited

Definition at line 198 of file SinglePhaseFluidProperties.h.

◆ p [5/9]

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

inherited

Definition at line 200 of file SinglePhaseFluidProperties.h.

◆ p [6/9]

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

inherited

Definition at line 202 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 208 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 212 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 214 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 217 of file SinglePhaseFluidProperties.h.

◆ rho

e e e e s T SinglePhaseFluidProperties::rho

inherited

Definition at line 194 of file SinglePhaseFluidProperties.h.

◆ T [1/2]

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

inherited

Definition at line 204 of file SinglePhaseFluidProperties.h.

◆ T [2/2]

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

inherited

Definition at line 206 of file SinglePhaseFluidProperties.h.

◆ v [1/5]

SinglePhaseFluidProperties::v

inherited

Definition at line 182 of file SinglePhaseFluidProperties.h.

◆ v [2/5]

e SinglePhaseFluidProperties::v

inherited

Definition at line 184 of file SinglePhaseFluidProperties.h.

◆ v [3/5]

e e SinglePhaseFluidProperties::v

inherited

Definition at line 186 of file SinglePhaseFluidProperties.h.

◆ v [4/5]

e e e SinglePhaseFluidProperties::v

inherited

Definition at line 188 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 216 of file SinglePhaseFluidProperties.h.

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

fluid_properties/include/fluidproperties/HelmholtzFluidProperties.h
fluid_properties/src/fluidproperties/HelmholtzFluidProperties.C

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

Detailed Description

Constructor & Destructor Documentation

◆ HelmholtzFluidProperties()

Member Function Documentation

◆ alpha()

◆ c_from_p_T()

◆ cp_from_p_T()

◆ criticalDensity()

◆ criticalInternalEnergy()

◆ criticalPressure()

◆ criticalTemperature()

◆ cv_from_p_T()

◆ d2alpha_ddelta2()

◆ d2alpha_ddeltatau()

◆ d2alpha_dtau2()

◆ dalpha_ddelta()

◆ dalpha_dtau()

◆ e_from_p_T() [1/2]

◆ e_from_p_T() [2/2]

◆ e_spndl_from_v()

◆ execute()

◆ finalize()

◆ h_from_p_T() [1/2]

◆ h_from_p_T() [2/2]

◆ henryCoefficients()

◆ initialize()

◆ makeZeroAndOne() [1/2]

◆ makeZeroAndOne() [2/2]

◆ molarMass()

◆ p_from_rho_T()

◆ p_T_from_h_s()

◆ p_T_from_v_e()

◆ p_T_from_v_h()

◆ propfunc() [1/14]

◆ propfunc() [2/14]

◆ propfunc() [3/14]

◆ propfunc() [4/14]

◆ propfunc() [5/14]

◆ propfunc() [6/14]

◆ propfunc() [7/14]

◆ propfunc() [8/14]

◆ propfunc() [9/14]

◆ propfunc() [10/14]

◆ propfunc() [11/14]

◆ propfunc() [12/14]

◆ propfunc() [13/14]

◆ propfunc() [14/14]

◆ propfuncWithDefault() [1/4]

◆ propfuncWithDefault() [2/4]

◆ propfuncWithDefault() [3/4]

◆ propfuncWithDefault() [4/4]

◆ rho_e_from_p_T()

◆ rho_from_p_T() [1/2]

◆ rho_from_p_T() [2/2]

◆ rho_mu_from_p_T() [1/3]

◆ rho_mu_from_p_T() [2/3]

◆ rho_mu_from_p_T() [3/3]

◆ s_from_p_T() [1/2]

◆ s_from_p_T() [2/2]

◆ subdomainSetup()

◆ threadJoin()

◆ triplePointPressure()

◆ triplePointTemperature()

◆ v_e_from_p_T() [1/2]

◆ v_e_from_p_T() [2/2]

◆ v_e_spndl_from_T()

◆ validParams()

◆ vaporPressure() [1/3]

◆ vaporPressure() [2/3]

◆ vaporPressure() [3/3]

◆ vaporTemperature() [1/3]