Fluid properties for (Lead) [Fazio]. More...

#include <LeadFluidProperties.h>

Inheritance diagram for LeadFluidProperties:

Public Types
typedef DataFileName	DataFileParameterType

Public Member Functions
	LeadFluidProperties (const InputParameters &parameters)

virtual std::string	fluidName () const override
	Fluid name. More...

Real	molarMass () const override
	Molar mass [kg/mol]. More...

Real	p_from_v_e (Real v, Real e) const override

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

Real	T_from_v_e (Real v, Real e) const override

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

Real	T_from_p_h (Real p, Real h) const override

void	T_from_p_h (Real p, Real h, Real &T, Real &dT_dp, Real &dT_dh) const override

Real	T_from_p_rho (Real p, Real rho) const
	Temperature from pressure and density. More...

void	T_from_p_rho (Real p, Real rho, Real &T, Real &dT_dp, Real &dT_drho) const

Real	cp_from_v_e (Real v, Real e) const override

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

Real	cv_from_v_e (Real v, Real e) const override

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

Real	cv_from_p_T (Real p, Real T) const override

void	cv_from_p_T (Real p, Real T, Real &cv, Real &dcp_dp, Real &dcp_dT) const override

Real	mu_from_v_e (Real v, Real e) const override

void	mu_from_v_e (Real v, Real e, Real &mu, Real &dmu_dv, Real &dmu_de) const override

Real	k_from_v_e (Real v, Real e) const override

void	k_from_v_e (Real v, Real e, Real &k, Real &dk_dv, Real &dk_de) const override

Real	rho_from_p_T (Real p, Real T) const override

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

void	rho_from_p_T (const ADReal &p, const ADReal &T, ADReal &rho, ADReal &drho_dp, ADReal &drho_dT) const override

Real	v_from_p_T (Real p, Real T) const override

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

Real	h_from_p_T (Real p, Real T) const override

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

Real	h_from_v_e (Real v, Real e) const override

void	h_from_v_e (Real v, Real e, Real &h, Real &dh_dv, Real &dh_de) const override

Real	e_from_p_T (Real p, Real T) const override

Real	e_from_p_rho (Real p, Real rho) const override

void	e_from_p_rho (Real p, Real rho, Real &e, Real &de_dp, Real &de_drho) const override

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

Real	cp_from_p_T (Real p, Real T) const override

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

Real	k_from_p_T (Real p, Real T) const override

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

Real	mu_from_p_T (Real p, Real T) const override

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

Real	bulk_modulus_from_p_T (Real p, Real T) const
	Isentropic bulk modulus from pressure and temperature. More...

Real	c_from_v_e (Real v, Real e) const override

ADReal	c_from_v_e (const ADReal &v, const ADReal &e) const override

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

virtual ADReal	vaporPressure (const ADReal &T) const

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

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

virtual ADReal	vaporTemperature (const ADReal &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 ADReal &p, const ADReal &T, ADReal &rho, ADReal &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

virtual Real	spatialValue (const Point &) const

virtual const std::vector< Point >	spatialPoints () const

void	setPrimaryThreadCopy (UserObject *primary)

UserObject *	primaryThreadCopy ()

SubProblem &	getSubProblem () const

bool	shouldDuplicateInitialExecution () const

void	gatherSum (T &value)

void	gatherMax (T &value)

void	gatherMin (T &value)

void	gatherProxyValueMax (T1 &proxy, T2 &value)

void	gatherProxyValueMin (T1 &proxy, T2 &value)

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

bool	isKokkosObject () const

MooseApp &	getMooseApp () const

const std::string &	type () const

const std::string &	name () const

std::string	typeAndName () const

MooseObjectParameterName	uniqueParameterName (const std::string &parameter_name) const

MooseObjectName	uniqueName () const

const InputParameters &	parameters () const

const hit::Node *	getHitNode () const

bool	hasBase () const

const std::string &	getBase () 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 *	queryParam (const std::string &name) 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	haveParameter (const std::string &name) const

bool	isParamValid (const std::string &name) const

bool	isParamSetByUser (const std::string &name) const

void	connectControllableParams (const std::string &parameter, const std::string &object_type, const std::string &object_name, const std::string &object_parameter) const

void	paramError (const std::string &param, Args... args) const

void	paramWarning (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

std::string	messagePrefix (const bool hit_prefix=true) const

std::string	errorPrefix (const std::string &) const

void	mooseError (Args &&... args) const

void	mooseDocumentedError (const std::string &repo_name, const unsigned int issue_num, Args &&... args) const

void	mooseErrorNonPrefixed (Args &&... args) const

void	mooseWarning (Args &&... args) const

void	mooseWarning (Args &&... args) const

void	mooseWarningNonPrefixed (Args &&... args) const

void	mooseWarningNonPrefixed (Args &&... args) const

void	mooseDeprecated (Args &&... args) const

void	mooseDeprecated (Args &&... args) const

void	mooseDeprecatedNoTrace (Args &&... args) const

void	mooseInfo (Args &&... args) const

void	callMooseError (std::string msg, const bool with_prefix, const hit::Node *node=nullptr, const bool show_trace=true) const

std::string	getDataFileName (const std::string &param) const

std::string	getDataFileNameByName (const std::string &relative_path) const

std::string	getDataFilePath (const std::string &relative_path) 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 UserObjectBase &	getUserObjectBase (const std::string &param_name, bool is_dependency=true) const

const UserObjectBase &	getUserObjectBaseByName (const UserObjectName &object_name, bool is_dependency=true) const

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

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

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

Moose::Kokkos::MaterialProperty< T, dimension >	getKokkosMaterialPropertyByName (const std::string &prop_name_in)

Moose::Kokkos::MaterialProperty< T, dimension >	getKokkosMaterialPropertyOldByName (const std::string &prop_name)

Moose::Kokkos::MaterialProperty< T, dimension >	getKokkosMaterialPropertyOlderByName (const std::string &prop_name)

Moose::Kokkos::MaterialProperty< T, dimension >	getKokkosMaterialProperty (const std::string &name)

Moose::Kokkos::MaterialProperty< T, dimension >	getKokkosMaterialPropertyOld (const std::string &name)

Moose::Kokkos::MaterialProperty< T, dimension >	getKokkosMaterialPropertyOlder (const std::string &name)

std::pair< const MaterialProperty< T > *, std::set< SubdomainID > >	getBlockMaterialProperty (const MaterialPropertyName &name)

std::pair< Moose::Kokkos::MaterialProperty< T, dimension >, std::set< SubdomainID > >	getKokkosBlockMaterialProperty (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)

virtual bool	getMaterialPropertyCalled () const

virtual 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 ()

Moose::StateArg	determineState () 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	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	hasKokkosMaterialProperty (const std::string &name)

bool	hasKokkosMaterialProperty (const std::string &name)

bool	hasKokkosMaterialPropertyByName (const std::string &name)

bool	hasKokkosMaterialPropertyByName (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

Moose::Kokkos::Function	getKokkosFunction (const std::string &name) const

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

Moose::Kokkos::Function	getKokkosFunctionByName (const FunctionName &name) const

const T &	getKokkosFunctionByName (const FunctionName &name) const

bool	hasKokkosFunction (const std::string &param_name) const

bool	hasKokkosFunctionByName (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 ()

virtual void	meshDisplaced ()

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	callMooseError (MooseApp const app, const InputParameters &params, std::string msg, const bool with_prefix, const hit::Node node, const bool show_trace=true)

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, NameFunc &&name_func)

static void	cyclicDependencyError (CyclicDependencyException< T2 > &e, const std::string &header)

Public Attributes
	usingCombinedWarningSolutionWarnings

const ConsoleStream	_console

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

static const std::string	type_param

static const std::string	name_param

static const std::string	unique_name_param

static const std::string	app_param

static const std::string	moose_base_param

static const std::string	kokkos_object_param

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 void	addPostprocessorDependencyHelper (const PostprocessorName &name) const override

virtual void	addVectorPostprocessorDependencyHelper (const VectorPostprocessorName &name) const override

virtual void	addUserObjectDependencyHelper (const UserObjectBase &uo) const override

void	addReporterDependencyHelper (const ReporterName &reporter_name) override

void	flagInvalidSolutionInternal (const InvalidSolutionID invalid_solution_id) const

InvalidSolutionID	registerInvalidSolutionInternal (const std::string &message, const bool warning) const

const ReporterContextBase &	getReporterContextBaseByName (const ReporterName &reporter_name) const

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

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

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

libMesh::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

virtual void	checkMaterialProperty (const std::string &name, const unsigned int state)

virtual void	getKokkosMaterialPropertyHook (const std::string &, const unsigned int)

void	markMatPropRequested (const std::string &)

MaterialPropertyName	getMaterialPropertyName (const std::string &name) const

void	checkExecutionStage ()

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)

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. More...

const Real	_T_initial_guess
	Initial guess for temperature (or temperature used to compute the initial guess) More...

const Real	_p_initial_guess
	Initial guess for pressure (or pressure used to compute the initial guess) More...

const unsigned int	_max_newton_its
	Maximum number of iterations for the variable conversion newton solves. More...

const bool	_verbose_newton
	Whether to output information about newton solves to console. More...

const Real	_T_c2k
	Conversion of temperature from Celsius to Kelvin. More...

const bool	_allow_imperfect_jacobians
	Flag to set unimplemented Jacobian entries to zero. More...

const Moose::CoordinateSystemType &	_coord_sys

const THREAD_ID	_tid

SubProblem &	_subproblem

FEProblemBase &	_fe_problem

SystemBase &	_sys

Assembly &	_assembly

const bool	_duplicate_initial_execution

std::set< std::string >	_depend_uo

const bool &	_enabled

MooseApp &	_app

Factory &	_factory

ActionFactory &	_action_factory

const std::string &	_type

const std::string &	_name

const InputParameters &	_pars

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 &	_mdi_feproblem

MooseApp &	_pg_moose_app

const std::string	_prefix

FEProblemBase &	_sc_fe_problem

const THREAD_ID	_sc_tid

const Real &	_real_zero

const VariableValue &	_scalar_zero

const Point &	_point_zero

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 bool	_is_kokkos_object

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

const Real &	_t_old

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

Static Private Attributes
static constexpr Real	_T_mo = 600.6
	Melting temperature of Lead. More...

	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	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	propfuncWithDefault (h, v, e) propfunc(g

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

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

e e e e s T T T T T rho v v T e p T	propfuncWithDefault (v, p, T) propfuncWithDefault(e

e e e e s T T T T T rho v v T e p T T	propfuncWithDefault (gamma, v, e) propfuncWithDefault(gamma

	v

e	v

e e	v

e e e	v

e e e e s T T T T T rho v v 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 e p	p

e e e e s T T T T T rho v v T e p T	p

e e e e s T T T T T rho v v T e p T T	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 e	h

Detailed Description

Fluid properties for (Lead) [Fazio].

Definition at line 17 of file LeadFluidProperties.h.

Constructor & Destructor Documentation

◆ LeadFluidProperties()

LeadFluidProperties::LeadFluidProperties ( const InputParameters & parameters )

Definition at line 23 of file LeadFluidProperties.C.

   : SinglePhaseFluidProperties(parameters)
 {
 }

Member Function Documentation

◆ bulk_modulus_from_p_T()

Real LeadFluidProperties::bulk_modulus_from_p_T	(	Real	p,
		Real	T
	)		const

Isentropic bulk modulus from pressure and temperature.

Parameters

p	pressure (Pa)
T	temperature (K)

Returns: Bulk Modules (N/m^2)

Definition at line 41 of file LeadFluidProperties.C.

Referenced by cv_from_p_T().

 {
   // Isentropic bulk modulus, eq 2.42 from Handbook
   return (43.50 - 1.552e-2 * T + 1.622e-6 * T * T) * 1e9;
 }

◆ c_from_v_e() [1/2]

Real LeadFluidProperties::c_from_v_e	(	Real	v,
		Real	e
	)		const

override

Definition at line 48 of file LeadFluidProperties.C.

 {
   auto T = T_from_v_e(v, e);
   return 1953 - 0.246 * T;
 }

◆ c_from_v_e() [2/2]

ADReal LeadFluidProperties::c_from_v_e	(	const ADReal &	v,
		const ADReal &	e
	)		const

override

Definition at line 55 of file LeadFluidProperties.C.

 {
   ADReal T = SinglePhaseFluidProperties::T_from_v_e(v, e);
   return 1953 - 0.246 * T;
 }

◆ cp_from_p_T() [1/2]

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

override

Definition at line 359 of file LeadFluidProperties.C.

Referenced by cp_from_p_T(), cv_from_p_T(), and h_from_p_T().

 {
   return 176.2 - 4.923e-2 * T + 1.544e-5 * T * T - 1.524e+6 / T / T;
 }

◆ cp_from_p_T() [2/2]

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

override

Definition at line 365 of file LeadFluidProperties.C.

 {
   cp = cp_from_p_T(p, T);
   dcp_dp = 0;
   dcp_dT = -4.923e-2 + 2 * 1.544e-5 * T + 2 * 1.524e6 / T / T / T;
 }

◆ cp_from_v_e() [1/2]

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

override

Definition at line 373 of file LeadFluidProperties.C.

Referenced by cp_from_v_e(), and h_from_v_e().

 {
   Real T = T_from_v_e(v, e);
   return 176.2 - 4.923e-2 * T + 1.544e-5 * T * T - 1.524e6 / T / T;
 }

◆ cp_from_v_e() [2/2]

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

override

Definition at line 380 of file LeadFluidProperties.C.

 {
   Real T, dT_dv, dT_de;
   T_from_v_e(v, e, T, dT_dv, dT_de);
   cp = cp_from_v_e(v, e);
   dcp_dv = -4.923e-2 * dT_dv + 2 * dT_dv * 1.544e-5 * T + 2 * dT_dv * 1.524e+6 / T / T / T;
 
   dcp_de = -4.923e-2 * dT_de + 2 * dT_de * 1.544e-5 * T + 2 * dT_de * 1.524e+6 / T / T / T;
 }

◆ criticalDensity()

Real SinglePhaseFluidProperties::criticalDensity ( ) const

virtualinherited

Critical density.

Returns: critical density (kg/m^3)

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

Definition at line 314 of file SinglePhaseFluidProperties.C.

Referenced by HelmholtzFluidProperties::c_from_p_T(), HelmholtzFluidProperties::cp_from_p_T(), TabulatedFluidProperties::criticalDensity(), SinglePhaseFluidProperties::criticalInternalEnergy(), HelmholtzFluidProperties::cv_from_p_T(), HelmholtzFluidProperties::e_from_p_T(), HelmholtzFluidProperties::h_from_p_T(), HelmholtzFluidProperties::p_from_rho_T(), HelmholtzFluidProperties::rho_from_p_T(), and HelmholtzFluidProperties::s_from_p_T().

 {
   return rho_from_p_T(criticalPressure(), criticalTemperature());
 }

◆ 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 320 of file SinglePhaseFluidProperties.C.

 {
   return e_from_p_rho(criticalPressure(), criticalDensity());
 }

◆ criticalPressure()

Real SinglePhaseFluidProperties::criticalPressure ( ) const

virtualinherited

Critical pressure.

Returns: critical pressure (Pa)

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

Definition at line 302 of file SinglePhaseFluidProperties.C.

Referenced by SinglePhaseFluidProperties::criticalDensity(), SinglePhaseFluidProperties::criticalInternalEnergy(), and TabulatedFluidProperties::criticalPressure().

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

◆ criticalTemperature()

Real SinglePhaseFluidProperties::criticalTemperature ( ) const

virtualinherited

Critical temperature.

Returns: critical temperature (K)

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

Definition at line 308 of file SinglePhaseFluidProperties.C.

Referenced by HelmholtzFluidProperties::c_from_p_T(), HelmholtzFluidProperties::cp_from_p_T(), SinglePhaseFluidProperties::criticalDensity(), TabulatedFluidProperties::criticalTemperature(), HelmholtzFluidProperties::cv_from_p_T(), HelmholtzFluidProperties::e_from_p_T(), HelmholtzFluidProperties::h_from_p_T(), HelmholtzFluidProperties::p_from_rho_T(), HelmholtzFluidProperties::rho_from_p_T(), HelmholtzFluidProperties::s_from_p_T(), and IdealRealGasMixtureFluidProperties::xs_prim_from_p_T().

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

◆ cv_from_p_T() [1/2]

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

override

Definition at line 412 of file LeadFluidProperties.C.

Referenced by cv_from_p_T(), and cv_from_v_e().

 {
   Real rho, drho_dT, drho_dp;
   rho_from_p_T(p, T, rho, drho_dp, drho_dT);
   Real alpha = -drho_dT / rho;
   Real bulk_modulus = bulk_modulus_from_p_T(p, T);
   Real cp = cp_from_p_T(p, T);
   return cp / (1 + alpha * alpha * bulk_modulus * T / rho / cp);
 }

◆ cv_from_p_T() [2/2]

void LeadFluidProperties::cv_from_p_T	(	Real	p,
		Real	T,
		Real &	cv,
		Real &	dcp_dp,
		Real &	dcp_dT
	)		const

override

Definition at line 423 of file LeadFluidProperties.C.

 {
   Real cp, dcp_dp, dcp_dT;
   cp_from_p_T(p, T, cp, dcp_dp, dcp_dT);
   cv = cv_from_p_T(p, T);
 
   Real rho, drho_dT, drho_dp;
   rho_from_p_T(p, T, rho, drho_dp, drho_dT);
   Real alpha = -drho_dT / rho;
   Real alpha_2 = alpha * alpha, alpha_3 = alpha * alpha * alpha;
   Real dalpha_dT = drho_dT * drho_dT / rho / rho;
   Real bulk = bulk_modulus_from_p_T(p, T);
   Real dbulk_dT = (-1.552e-2 + 2 * 1.622e-6 * T) * 1e9;
   Real denominator = (1 + alpha * alpha * bulk * T / rho / cp);
   // no pressure dependence in alpha, T, bulk modulus, cp or rho
   dcv_dp = 0;
   dcv_dT = dcp_dT / denominator -
            cp / denominator / denominator *
                (2 * alpha * dalpha_dT * bulk * T / rho / cp + alpha_2 * dbulk_dT * T / rho / cp +
                 alpha_2 * bulk / rho / cp + alpha_3 * bulk * T / rho / cp -
                 dcp_dT * alpha_2 * bulk * T / rho / cp / cp);
 }

◆ cv_from_v_e() [1/2]

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

override

Definition at line 391 of file LeadFluidProperties.C.

 {
   Real p = p_from_v_e(v, e);
   Real T = T_from_v_e(v, e);
   return cv_from_p_T(p, T);
 }

◆ cv_from_v_e() [2/2]

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

override

Definition at line 399 of file LeadFluidProperties.C.

 {
   Real p, dp_dv, dp_de;
   p_from_v_e(v, e, p, dp_dv, dp_de);
   Real T, dT_dv, dT_de;
   T_from_v_e(v, e, T, dT_dv, dT_de);
   Real dcv_dp, dcv_dT;
   cv_from_p_T(p, T, cv, dcv_dp, dcv_dT);
   dcv_dv = dcv_dp * dp_dv + dcv_dT * dT_dv;
   dcv_de = dcv_dp * dp_de + dcv_dT * dT_de;
 }

◆ e_from_p_rho() [1/2]

Real LeadFluidProperties::e_from_p_rho	(	Real	p,
		Real	rho
	)		const

override

Definition at line 207 of file LeadFluidProperties.C.

 {
   return e_from_p_T(p, T_from_p_rho(p, rho));
 }

◆ e_from_p_rho() [2/2]

void LeadFluidProperties::e_from_p_rho	(	Real	p,
		Real	rho,
		Real &	e,
		Real &	de_dp,
		Real &	de_drho
	)		const

override

Definition at line 213 of file LeadFluidProperties.C.

 {
   Real T, dT_dp, dT_drho;
   T_from_p_rho(p, rho, T, dT_dp, dT_drho);
   Real de_dp_T, de_dT;
   e_from_p_T(p, T, e, de_dp_T, de_dT);
   de_dp = de_dp_T * 1 + de_dT * dT_dp;
   de_drho = de_dT * dT_drho;
 }

◆ e_from_p_T() [1/2]

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

override

Definition at line 187 of file LeadFluidProperties.C.

Referenced by e_from_p_rho(), and e_from_p_T().

 {
   // definition of h = e + p * v
   Real v = v_from_p_T(p, T);
   Real h = h_from_p_T(p, T);
   return h - p * v;
 }

◆ e_from_p_T() [2/2]

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

override

Definition at line 196 of file LeadFluidProperties.C.

 {
   Real dh_dp, dv_dp, dh_dT, dv_dT, v, h;
   h_from_p_T(p, T, h, dh_dp, dh_dT);
   v_from_p_T(p, T, v, dv_dp, dv_dT);
   e = e_from_p_T(p, T);
   de_dp = dh_dp - v - dv_dp * p;
   de_dT = dh_dT - dv_dT * p;
 }

◆ 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 483 of file SinglePhaseFluidProperties.C.

 {
   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 {}

◆ fluidName()

std::string LeadFluidProperties::fluidName ( ) const

overridevirtual

Fluid name.

Returns: string representing fluid name

Reimplemented from SinglePhaseFluidProperties.

Definition at line 29 of file LeadFluidProperties.C.

 {
   return "Lead";
 }

◆ h_from_p_T() [1/2]

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

override

Definition at line 150 of file LeadFluidProperties.C.

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

 {
   // see 2.53 in 2005 NEA Lead Handbook
   // 5.1467e-6 is replaced by 1.544e-5/3 for accuracy
   return 176.2 * (T - _T_mo) - 2.4615e-2 * (T * T - _T_mo * _T_mo) +
          (1.544e-5 / 3) * (T * T * T - _T_mo * _T_mo * _T_mo) + 1.524e+6 * (1 / T - 1 / _T_mo);
 }

◆ h_from_p_T() [2/2]

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

override

Definition at line 159 of file LeadFluidProperties.C.

 {
   h = h_from_p_T(p, T);
   Real cp = cp_from_p_T(p, T);
   dh_dp = 0;
   dh_dT = cp;
 }

◆ h_from_v_e() [1/2]

Real LeadFluidProperties::h_from_v_e	(	Real	v,
		Real	e
	)		const

override

Definition at line 168 of file LeadFluidProperties.C.

Referenced by h_from_v_e(), and p_from_v_e().

 {
   Real T = T_from_v_e(v, e);
   return 176.2 * (T - _T_mo) - 2.4615e-2 * (T * T - _T_mo * _T_mo) +
          (1.544e-5 / 3) * (T * T * T - _T_mo * _T_mo * _T_mo) + 1.524e+6 * (1 / T - 1 / _T_mo);
 }

◆ h_from_v_e() [2/2]

void LeadFluidProperties::h_from_v_e	(	Real	v,
		Real	e,
		Real &	h,
		Real &	dh_dv,
		Real &	dh_de
	)		const

override

Definition at line 176 of file LeadFluidProperties.C.

 {
   Real T, dT_dv, dT_de;
   T_from_v_e(v, e, T, dT_dv, dT_de);
   h = h_from_v_e(v, e);
   Real cp = cp_from_v_e(v, e);
   dh_dv = cp * dT_dv;
   dh_de = cp * dT_de;
 }

◆ 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 378 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 {}

◆ k_from_p_T() [1/2]

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

override

Definition at line 461 of file LeadFluidProperties.C.

Referenced by k_from_p_T().

 {
   return 0.011 * T + 9.2;
 }

◆ k_from_p_T() [2/2]

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

override

Definition at line 467 of file LeadFluidProperties.C.

 {
   k = k_from_p_T(p, T);
   dk_dp = 0;
   dk_dT = 0.011;
 }

◆ k_from_v_e() [1/2]

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

override

Definition at line 96 of file LeadFluidProperties.C.

Referenced by k_from_v_e().

 {
   Real T = T_from_v_e(v, e);
   return 0.011 * T + 9.2;
 }

◆ k_from_v_e() [2/2]

void LeadFluidProperties::k_from_v_e	(	Real	v,
		Real	e,
		Real &	k,
		Real &	dk_dv,
		Real &	dk_de
	)		const

override

Definition at line 103 of file LeadFluidProperties.C.

 {
   Real T, dT_dv, dT_de;
   T_from_v_e(v, e, T, dT_dv, dT_de);
   k = k_from_v_e(v, e);
   dk_dv = 0.011 * dT_dv;
   dk_de = 0.011 * dT_de;
 }

◆ 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 478 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 485 of file SinglePhaseFluidProperties.h.

 {
   return {Real{0}, Real{1}};
 }

◆ molarMass()

Real LeadFluidProperties::molarMass ( ) const

overridevirtual

Molar mass [kg/mol].

Returns: molar mass

Reimplemented from SinglePhaseFluidProperties.

Definition at line 35 of file LeadFluidProperties.C.

 {
   return 2.072e-1;
 }

◆ mu_from_p_T() [1/2]

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

override

Definition at line 447 of file LeadFluidProperties.C.

Referenced by mu_from_p_T().

 {
   return 4.55e-4 * std::exp(1069 / T);
 }

◆ mu_from_p_T() [2/2]

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

override

Definition at line 453 of file LeadFluidProperties.C.

 {
   mu = mu_from_p_T(p, T);
   dmu_dp = 0;
   dmu_dT = -1069 * 4.55e-4 * std::exp(1069 / T) / T / T;
 }

◆ mu_from_v_e() [1/2]

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

override

Definition at line 79 of file LeadFluidProperties.C.

Referenced by mu_from_v_e().

 {
   Real T = T_from_v_e(v, e);
   return 4.55e-4 * std::exp(1069 / T);
 }

◆ mu_from_v_e() [2/2]

void LeadFluidProperties::mu_from_v_e	(	Real	v,
		Real	e,
		Real &	mu,
		Real &	dmu_dv,
		Real &	dmu_de
	)		const

override

Definition at line 86 of file LeadFluidProperties.C.

 {
   Real T, dT_dv, dT_de;
   T_from_v_e(v, e, T, dT_dv, dT_de);
   mu = mu_from_v_e(v, e);
   dmu_dv = dT_dv * -1069 * 4.55e-4 * exp(1069 / T) / T / T;
   dmu_de = dT_de * -1069 * 4.55e-4 * exp(1069 / T) / T / T;
 }

◆ p_from_v_e() [1/2]

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

override

Definition at line 62 of file LeadFluidProperties.C.

Referenced by cv_from_v_e(), and p_from_v_e().

 {
   Real h = h_from_v_e(v, e);
   return (h - e) / v;
 }

◆ p_from_v_e() [2/2]

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

override

Definition at line 69 of file LeadFluidProperties.C.

 {
   Real h, dh_dv, dh_de;
   h_from_v_e(v, e, h, dh_dv, dh_de);
   p = p_from_v_e(v, e);
   dp_dv = (v * dh_dv - h + e) / v / v;
   dp_de = (dh_de - 1) / v;
 }

◆ 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 599 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,
                                         "p_T_from_h_s",
                                         _max_newton_its,
                                         _verbose_newton);
     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 513 of file SinglePhaseFluidProperties.h.

Referenced by TabulatedBicubicFluidProperties::constructInterpolation(), TemperaturePressureFunctionFluidProperties::cp_from_v_e(), TemperaturePressureFunctionFluidProperties::cv_from_v_e(), TabulatedFluidProperties::g_from_v_e(), TemperaturePressureFunctionFluidProperties::k_from_v_e(), TemperaturePressureFunctionFluidProperties::mu_from_v_e(), and TemperaturePressureFunctionFluidProperties::T_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,
                                         "p_T_from_v_e",
                                         _max_newton_its,
                                         _verbose_newton);
     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 559 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,
                                         "p_T_from_v_h",
                                         _max_newton_its,
                                         _verbose_newton);
     conversion_succeeded = true;
   }
   catch (MooseException &)
   {
     conversion_succeeded = false;
   }
 
   if (!conversion_succeeded)
     mooseDoOnce(mooseWarning("Conversion from (v, h)=(", v, ", ", h, ") to (p, T) failed"));
 }

◆ propfunc() [1/12]

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(ADReal a, ADReal b) and x_from_a_b(ADReal a, ADReal b, ADReal x, ADReal dx_da, ADReal 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() [2/12]

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

inherited

◆ propfunc() [3/12]

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

inherited

◆ propfunc() [4/12]

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

inherited

◆ propfunc() [5/12]

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

inherited

◆ propfunc() [6/12]

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

inherited

◆ propfunc() [7/12]

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

inherited

◆ propfunc() [8/12]

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

inherited

◆ propfunc() [9/12]

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

inherited

◆ propfunc() [10/12]

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

inherited

◆ propfunc() [11/12]

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

inherited

◆ propfunc() [12/12]

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

inherited

◆ propfuncWithDefault() [1/7]

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

inherited

◆ propfuncWithDefault() [2/7]

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

inherited

◆ propfuncWithDefault() [3/7]

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

inherited

◆ propfuncWithDefault() [4/7]

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

inherited

◆ propfuncWithDefault() [5/7]

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

inherited

◆ propfuncWithDefault() [6/7]

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

inherited

◆ propfuncWithDefault() [7/7]

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

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 438 of file SinglePhaseFluidProperties.C.

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

◆ rho_from_p_T() [1/3]

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

override

Definition at line 113 of file LeadFluidProperties.C.

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

 {
   return 11441 - 1.2795 * T;
 }

◆ rho_from_p_T() [2/3]

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

override

Definition at line 119 of file LeadFluidProperties.C.

 {
   rho = rho_from_p_T(p, T);
   drho_dp = 0;
   drho_dT = -1.2795;
 }

◆ rho_from_p_T() [3/3]

void LeadFluidProperties::rho_from_p_T	(	const ADReal &	p,
		const ADReal &	T,
		ADReal &	rho,
		ADReal &	drho_dp,
		ADReal &	drho_dT
	)		const

override

Definition at line 127 of file LeadFluidProperties.C.

 {
   rho = SinglePhaseFluidProperties::rho_from_p_T(p, T);
   drho_dp = 0;
   drho_dT = -1.2795;
 }

◆ 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 452 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 459 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 ADReal &	p,
		const ADReal &	T,
		ADReal &	rho,
		ADReal &	mu
	)		const

virtualinherited

Definition at line 473 of file SinglePhaseFluidProperties.C.

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

◆ subdomainSetup()

virtual void FluidProperties::subdomainSetup ( )

inlinefinalvirtualinherited

Reimplemented from ThreadedGeneralUserObject.

Definition at line 38 of file FluidProperties.h.

38 {}

◆ T_from_p_h() [1/2]

Real LeadFluidProperties::T_from_p_h	(	Real	p,
		Real	h
	)		const

override

Definition at line 252 of file LeadFluidProperties.C.

Referenced by T_from_p_h().

 {
   // Obtained from sympy solving h(T) with T as a symbol
   return -2067.9254113598 *
              std::sqrt(
                  -7.36955226020901e-15 * (232320624.378877 * h - 74598764305248.3) /
                      std::pow(
                          6.71651186402396e-6 * h +
                              MathUtils::pow(1.0 - 3.99399123439419e-6 * h, 2) +
                              std::sqrt(0.702754599548161 *
                                            MathUtils::pow(3.11426907057403e-6 * h - 1.0, 3) +
                                        MathUtils::pow(
                                            -6.71651186402396e-6 * h -
                                                MathUtils::pow(1.0 - 3.99399123439419e-6 * h, 2) +
                                                0.0419568962265043,
                                            2)) -
                              0.0419568962265043,
                          1. / 3.) +
                  0.61835541884035 *
                      std::pow(
                          6.71651186402396e-6 * h +
                              MathUtils::pow(1.0 - 3.99399123439419e-6 * h, 2) +
                              std::sqrt(0.702754599548161 *
                                            MathUtils::pow(3.11426907057403e-6 * h - 1.0, 3) +
                                        MathUtils::pow(
                                            -6.71651186402396e-6 * h -
                                                MathUtils::pow(1.0 - 3.99399123439419e-6 * h, 2) +
                                                0.0419568962265043,
                                            2)) -
                              0.0419568962265043,
                          1. / 3.) -
                  1.0) +
          2924.48816272099 *
              std::sqrt(
                  7.0676560676229e-12 * (97296416908.1661 - 388601.036269178 * h) /
                      std::sqrt(
                          -7.36955226020901e-15 * (232320624.378877 * h - 74598764305248.3) /
                              std::pow(
                                  6.71651186402396e-6 * h +
                                      MathUtils::pow(1.0 - 3.99399123439419e-6 * h, 2) +
                                      std::sqrt(
                                          0.702754599548161 *
                                              MathUtils::pow(3.11426907057403e-6 * h - 1.0, 3) +
                                          MathUtils::pow(
                                              -6.71651186402396e-6 * h -
                                                  MathUtils::pow(1.0 - 3.99399123439419e-6 * h, 2) +
                                                  0.0419568962265043,
                                              2)) -
                                      0.0419568962265043,
                                  1. / 3.) +
                          0.61835541884035 *
                              std::pow(
                                  6.71651186402396e-6 * h +
                                      MathUtils::pow(1.0 - 3.99399123439419e-6 * h, 2) +
                                      std::sqrt(
                                          0.702754599548161 *
                                              MathUtils::pow(3.11426907057403e-6 * h - 1.0, 3) +
                                          MathUtils::pow(
                                              -6.71651186402396e-6 * h -
                                                  MathUtils::pow(1.0 - 3.99399123439419e-6 * h, 2) +
                                                  0.0419568962265043,
                                              2)) -
                                      0.0419568962265043,
                                  1. / 3.) -
                          1.0) +
                  3.6847761301045e-15 * (232320624.378877 * h - 74598764305248.3) /
                      std::pow(
                          6.71651186402396e-6 * h +
                              MathUtils::pow(1.0 - 3.99399123439419e-6 * h, 2) +
                              std::sqrt(0.702754599548161 *
                                            MathUtils::pow(3.11426907057403e-6 * h - 1.0, 3) +
                                        MathUtils::pow(
                                            -6.71651186402396e-6 * h -
                                                MathUtils::pow(1.0 - 3.99399123439419e-6 * h, 2) +
                                                0.0419568962265043,
                                            2)) -
                              0.0419568962265043,
                          1. / 3.) -
                  0.309177709420175 *
                      std::pow(
                          6.71651186402396e-6 * h +
                              MathUtils::pow(1.0 - 3.99399123439419e-6 * h, 2) +
                              std::sqrt(0.702754599548161 *
                                            MathUtils::pow(3.11426907057403e-6 * h - 1.0, 3) +
                                        MathUtils::pow(
                                            -6.71651186402396e-6 * h -
                                                MathUtils::pow(1.0 - 3.99399123439419e-6 * h, 2) +
                                                0.0419568962265043,
                                            2)) -
                              0.0419568962265043,
                          1. / 3.) -
                  1.0) +
          1195.67681347073;
 }

◆ T_from_p_h() [2/2]

void LeadFluidProperties::T_from_p_h	(	Real	p,
		Real	h,
		Real &	T,
		Real &	dT_dp,
		Real &	dT_dh
	)		const

override

Definition at line 348 of file LeadFluidProperties.C.

 {
   T = T_from_p_h(p, h);
   dT_dp = 0;
   // using inverse relation
   Real h1, dh_dp, dh_dT;
   h_from_p_T(p, T, h1, dh_dp, dh_dT);
   dT_dh = 1 / dh_dT;
 }

◆ T_from_p_rho() [1/2]

Real LeadFluidProperties::T_from_p_rho	(	Real	p,
		Real	rho
	)		const

Temperature from pressure and density.

Parameters

p	pressure (Pa)
rho	density (kg/m$^3$)

Returns: temperature (K)

Definition at line 224 of file LeadFluidProperties.C.

Referenced by e_from_p_rho(), and T_from_p_rho().

 {
   return (rho - 11441) / -1.2795;
 }

◆ T_from_p_rho() [2/2]

void LeadFluidProperties::T_from_p_rho	(	Real	p,
		Real	rho,
		Real &	T,
		Real &	dT_dp,
		Real &	dT_drho
	)		const

Definition at line 230 of file LeadFluidProperties.C.

 {
   T = T_from_p_rho(p, rho);
   dT_dp = 0;
   dT_drho = 1 / -1.2795;
 }

◆ T_from_v_e() [1/2]

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

override

Definition at line 238 of file LeadFluidProperties.C.

Referenced by c_from_v_e(), cp_from_v_e(), cv_from_v_e(), h_from_v_e(), k_from_v_e(), mu_from_v_e(), and T_from_v_e().

 {
   return (1 / v - 11441) / -1.2795;
 }

◆ T_from_v_e() [2/2]

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

override

Definition at line 244 of file LeadFluidProperties.C.

 {
   T = T_from_v_e(v, e);
   dT_de = 0;
   dT_dv = 1. / v / v / 1.2795;
 }

◆ 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 TabulatedFluidProperties, CO2FluidProperties, HydrogenFluidProperties, NitrogenFluidProperties, MethaneFluidProperties, NaClFluidProperties, and Water97FluidProperties.

Definition at line 326 of file SinglePhaseFluidProperties.C.

Referenced by TabulatedFluidProperties::triplePointPressure().

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

◆ triplePointTemperature()

Real SinglePhaseFluidProperties::triplePointTemperature ( ) const

virtualinherited

Triple point temperature.

Returns: triple point temperature (K)

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

Definition at line 332 of file SinglePhaseFluidProperties.C.

Referenced by TabulatedFluidProperties::triplePointTemperature().

 {
   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 639 of file SinglePhaseFluidProperties.h.

Referenced by TabulatedFluidProperties::h_from_p_T(), and TabulatedFluidProperties::s_from_p_T().

 {
   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 659 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 489 of file SinglePhaseFluidProperties.C.

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

◆ v_from_p_T() [1/2]

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

override

Definition at line 136 of file LeadFluidProperties.C.

Referenced by e_from_p_T(), and v_from_p_T().

 {
   return 1.0 / rho_from_p_T(p, T);
 }

◆ v_from_p_T() [2/2]

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

override

Definition at line 142 of file LeadFluidProperties.C.

 {
   v = v_from_p_T(p, T);
   dv_dp = 0;
   dv_dT = 1.2795 / MathUtils::pow(11441 - 1.2795 * T, 2);
 }

◆ validParams()

InputParameters LeadFluidProperties::validParams ( )

static

Definition at line 15 of file LeadFluidProperties.C.

 {
   InputParameters params = SinglePhaseFluidProperties::validParams();
   params.addClassDescription("Fluid properties for Lead");
 
   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, TabulatedFluidProperties, CO2FluidProperties, HydrogenFluidProperties, NitrogenFluidProperties, and MethaneFluidProperties.

Definition at line 372 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, TabulatedFluidProperties, CO2FluidProperties, HydrogenFluidProperties, NitrogenFluidProperties, and MethaneFluidProperties.

Definition at line 384 of file SinglePhaseFluidProperties.C.

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

◆ vaporPressure() [3/3]

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

virtualinherited

Definition at line 393 of file SinglePhaseFluidProperties.C.

 {
   Real p = 0.0;
   Real temperature = T.value();
   Real dpdT = 0.0;
 
   vaporPressure(temperature, p, dpdT);
 
   ADReal 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, and TabulatedFluidProperties.

Definition at line 408 of file SinglePhaseFluidProperties.C.

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

Definition at line 414 of file SinglePhaseFluidProperties.C.

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

◆ vaporTemperature() [3/3]

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

virtualinherited

Definition at line 423 of file SinglePhaseFluidProperties.C.

 {
   Real T = 0.0;
   Real pressure = p.value();
   Real dTdp = 0.0;
 
   vaporTemperature(pressure, T, dTdp);
 
   ADReal 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 492 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];
 }