Fluid properties provided as multiple-variable functions of temperature and pressure. More...

#include <TemperaturePressureFunctionFluidProperties.h>

Inheritance diagram for TemperaturePressureFunctionFluidProperties:

Public Types
typedef DataFileName	DataFileParameterType

Public Member Functions
	TemperaturePressureFunctionFluidProperties (const InputParameters &parameters)

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

virtual Real	T_from_v_e (Real v, Real e) const override
	Temperature from specific volume and specific internal energy. More...

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

virtual Real	T_from_p_h (Real p, Real h) const override
	Temperature from pressure and specific enthalpy. More...

virtual Real	p_from_v_e (Real v, Real e) const override
	Pressure from specific volume and specific internal energy. More...

virtual Real	cp_from_v_e (Real v, Real e) const override
	Isobaric specific heat from specific volume and specific internal energy. More...

virtual void	cp_from_v_e (Real v, Real e, Real &cp, Real &dcp_dv, Real &dcp_de) const override
	Isobaric specific heat capacity and its derivatives from specific volume and energy. More...

virtual Real	cv_from_v_e (Real v, Real e) const override
	Isochoric specific heat from specific volume and specific internal energy. More...

virtual void	cv_from_v_e (Real p, Real T, Real &cv, Real &dcv_dv, Real &dcv_de) const override
	Isochoric specific heat capacity and its derivatives from pressure and temperature. More...

virtual Real	mu_from_v_e (Real v, Real e) const override
	Dynamic viscosity from specific volume and specific internal energy. More...

virtual Real	k_from_v_e (Real v, Real e) const override
	Thermal conductivity from specific volume and specific internal energy. More...

virtual Real	rho_from_p_T (Real p, Real T) const override
	Density from pressure and temperature. More...

virtual void	rho_from_p_T (Real p, Real T, Real &rho, Real &drho_dp, Real &drho_dT) const override
	Density and its derivatives from pressure and temperature. More...

virtual void	rho_from_p_T (const ADReal &pressure, const ADReal &temperature, ADReal &rho, ADReal &drho_dp, ADReal &drho_dT) const override

virtual Real	v_from_p_T (Real p, Real T) const override
	Specific volume from pressure and temperature. More...

virtual void	v_from_p_T (Real p, Real T, Real &v, Real &dv_dp, Real &dv_dT) const override
	Specific volume and its derivatives from pressure and temperature. More...

virtual Real	h_from_p_T (Real p, Real T) const override
	Specific enthalpy from pressure and temperature. More...

virtual void	h_from_p_T (Real p, Real T, Real &h, Real &dh_dp, Real &dh_dT) const override
	Specific enthalpy and its derivatives from pressure and temperature. More...

virtual Real	e_from_p_T (Real p, Real T) const override
	Specific internal energy from pressure and temperature. More...

virtual void	e_from_p_T (Real p, Real T, Real &e, Real &de_dp, Real &de_dT) const override
	Specific internal energy and its derivatives from pressure and temperature. More...

virtual Real	e_from_p_rho (Real p, Real rho) const override
	Specific internal energy from pressure and density. More...

virtual Real	beta_from_p_T (Real p, Real T) const override
	Thermal expansion coefficient from pressure and temperature. More...

virtual Real	cp_from_p_T (Real p, Real T) const override
	Isobaric specific heat capacity from pressure and temperature. More...

virtual void	cp_from_p_T (Real p, Real T, Real &cp, Real &dcp_dp, Real &dcp_dT) const override
	Isobaric specific heat capacity and its derivatives from pressure and temperature. More...

virtual Real	cv_from_p_T (Real p, Real T) const override
	Isochoric specific heat capacity from pressure and temperature. More...

virtual void	cv_from_p_T (Real p, Real T, Real &cv, Real &dcv_dp, Real &dcv_dT) const override
	Isochoric specific heat capacity and its derivatives from pressure and temperature. More...

virtual Real	k_from_p_T (Real p, Real T) const override
	Thermal conductivity from pressure and temperature. More...

virtual void	k_from_p_T (Real p, Real T, Real &k, Real &dk_dp, Real &dk_dT) const override
	Thermal conductivity and its derivatives wrt pressure and temperature. More...

virtual Real	mu_from_p_T (Real p, Real T) const override
	Dynamic viscosity from pressure and temperature. More...

virtual void	mu_from_p_T (Real p, Real T, Real &mu, Real &dmu_drho, Real &dmu_dT) const override
	Dynamic viscosity and its derivatives wrt pressure and temperature. More...

Real	s_from_p_T (Real, Real) const override

void	s_from_p_T (Real, Real, Real &, Real &, Real &) const override

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

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

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 &proxy, T2 &value)

void	gatherProxyValueMin (T1 &proxy, T2 &value)

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 *	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	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 &relative_path) const

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

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 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)

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

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	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 ()

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	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
void	initialSetup () override
	Functions are constructed after fluid properties, so we delay the getting of the Function. 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

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)

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)

void	flagInvalidSolutionInternal (const InvalidSolutionID invalid_solution_id) const

InvalidSolutionID	registerInvalidSolutionInternal (const std::string &message, const bool warning) 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
bool	_initialized
	whether the object is initialized, eg, the functions have been retrieved from the problem More...

const Function *	_k_function
	function defining thermal conductivity as a function of temperature and pressure More...

const Function *	_rho_function
	function defining density as a function of temperature and pressure More...

const Function *	_mu_function
	function defining dynamic viscosity as a function of temperature and pressure More...

const Function *	_cp_function
	function defining specific heat as a function of temperature and pressure More...

const Real	_cv
	constant isochoric specific heat More...

const bool	_cv_is_constant
	whether a constant isochoric specific heat is used More...

const Real	_e_ref
	Reference specific energy. More...

const Real	_T_ref
	Reference temperature for the reference specific energy. More...

const Real	_integration_dT
	Size of temperature intervals when integrating the specific heat to compute the specific energy. More...

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 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 &	_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 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

	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 provided as multiple-variable functions of temperature and pressure.

Temperature is passed as the first spatial coordinate, x, to the function, while pressure is passed as the second spatial coordinate, y.

Definition at line 20 of file TemperaturePressureFunctionFluidProperties.h.

Constructor & Destructor Documentation

◆ TemperaturePressureFunctionFluidProperties()

TemperaturePressureFunctionFluidProperties::TemperaturePressureFunctionFluidProperties ( const InputParameters & parameters )

Definition at line 42 of file TemperaturePressureFunctionFluidProperties.C.

   : SinglePhaseFluidProperties(parameters),
     _initialized(false),
     _cv(getParam<Real>("cv")),
     _cv_is_constant(_cv != 0),
     _e_ref(getParam<Real>("e_ref")),
     _T_ref(getParam<Real>("T_ref")),
     _integration_dT(getParam<Real>("dT_integration_intervals"))
 {
   if (isParamValid("cp") && _cv_is_constant)
     paramError("cp", "The parameter 'cp' may only be specified if 'cv' is unspecified or is zero.");
 }

Member Function Documentation

◆ beta_from_p_T()

Real TemperaturePressureFunctionFluidProperties::beta_from_p_T	(	Real	p,
		Real	T
	)		const

overridevirtual

Thermal expansion coefficient from pressure and temperature.

Parameters

[in]	p	pressure (Pa)
[in]	T	temperature (K)

Returns: thermal expansion coefficient (1/K)

Definition at line 416 of file TemperaturePressureFunctionFluidProperties.C.

 {
   Real rho, drho_dp, drho_dT;
   rho_from_p_T(pressure, temperature, rho, drho_dp, drho_dT);
   return -drho_dT / rho;
 }

◆ cp_from_p_T() [1/2]

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

overridevirtual

Isobaric specific heat capacity from pressure and temperature.

Parameters

p	pressure (Pa)
T	temperature (K)

Returns: isobaric specific heat (J/kg/.K)

Definition at line 424 of file TemperaturePressureFunctionFluidProperties.C.

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

 {
   if (_cv_is_constant)
   {
     Real rho, drho_dp, drho_dT;
     rho_from_p_T(p, T, rho, drho_dp, drho_dT);
     // Wikipedia notation for thermal expansion / compressibility coefficients
     Real alpha = -drho_dT / rho;
     Real beta = -drho_dp / rho;
     return _cv + MathUtils::pow(alpha, 2) * T / rho / beta;
   }
   else
   {
     if (!_initialized)
       const_cast<TemperaturePressureFunctionFluidProperties *>(this)->initialSetup();
     return _cp_function->value(0, Point(T, p, 0));
   }
 }

◆ cp_from_p_T() [2/2]

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

overridevirtual

Isobaric specific heat capacity and its derivatives from pressure and temperature.

Parameters

[in]	p	pressure (Pa)
[in]	T	temperature (K)
[out]	cp	isobaric specific heat (J/kg/K)
[out]	dcp_dp	derivative of isobaric specific heat w.r.t. pressure (J/kg/K/Pa)
[out]	dcp_dT	derivative of isobaric specific heat w.r.t. temperature (J/kg/K/K)

Definition at line 444 of file TemperaturePressureFunctionFluidProperties.C.

 {
   if (_cv_is_constant)
   {
     cp = cp_from_p_T(pressure, temperature);
     Real eps = 1e-8;
     Real cp_1p = cp_from_p_T(pressure * (1 + eps), temperature);
     Real cp_1T = cp_from_p_T(pressure, temperature * (1 + eps));
     dcp_dp = (cp_1p - cp) / (pressure * eps);
     dcp_dT = (cp_1T - cp) / (temperature * eps);
   }
   else
   {
     cp = cp_from_p_T(pressure, temperature);
     const RealVectorValue grad_function =
         _cp_function->gradient(0, Point(temperature, pressure, 0));
     dcp_dT = grad_function(0);
     dcp_dp = grad_function(1);
   }
 }

◆ cp_from_v_e() [1/2]

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

overridevirtual

Isobaric specific heat from specific volume and specific internal energy.

Parameters

[in]	v	specific volume (m$^3$/kg)
[in]	e	specific internal energy (J/kg)

Returns: isobaric specific heat (J/kg.K)

Definition at line 128 of file TemperaturePressureFunctionFluidProperties.C.

Referenced by cp_from_v_e().

 {
   if (_cv_is_constant)
   {
     Real p = p_from_v_e(v, e);
     Real T = T_from_v_e(v, e);
     return cp_from_p_T(p, T);
   }
   else
   {
     const Real p0 = _p_initial_guess;
     const Real T0 = _T_initial_guess;
     Real p, T;
     bool conversion_succeeded = true;
     p_T_from_v_e(v, e, p0, T0, p, T, conversion_succeeded);
     if (conversion_succeeded)
       return cp_from_p_T(p, T);
     else
       mooseError("cp_from_v_e calculation failed. p= ", p, " T = ", T);
   }
 }

◆ cp_from_v_e() [2/2]

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

overridevirtual

Isobaric specific heat capacity and its derivatives from specific volume and energy.

Parameters

[in]	v	specific volume
[in]	e	specific energy
[out]	cp	isobaric specific heat (J/kg/K)
[out]	dcp_dv	derivative of isobaric specific heat w.r.t. specific volume
[out]	dcp_de	derivative of isobaric specific heat w.r.t. specific energy

Definition at line 151 of file TemperaturePressureFunctionFluidProperties.C.

 {
   cp = cp_from_v_e(v, e);
   // Using finite difference to get around difficulty of implementation
   Real eps = 1e-10;
   Real cp_pert = cp_from_v_e(v * (1 + eps), e);
   dcp_dv = (cp_pert - cp) / eps / v;
   cp_pert = cp_from_v_e(v, e * (1 + eps));
   dcp_de = (cp_pert - cp) / eps / e;
 }

◆ criticalDensity()

Real SinglePhaseFluidProperties::criticalDensity ( ) const

virtualinherited

Critical density.

Returns: critical density (kg/m^3)

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

Definition at line 310 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 316 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 298 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 IdealGasFluidProperties, TabulatedFluidProperties, CaloricallyImperfectGas, CO2FluidProperties, HydrogenFluidProperties, NitrogenFluidProperties, StiffenedGasFluidProperties, MethaneFluidProperties, TestSinglePhaseFluidProperties, NaClFluidProperties, and Water97FluidProperties.

Definition at line 304 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 TemperaturePressureFunctionFluidProperties::cv_from_p_T	(	Real	p,
		Real	T
	)		const

overridevirtual

Isochoric specific heat capacity from pressure and temperature.

Parameters

p	pressure (Pa)
T	temperature (K)

Returns: isochoric specific heat (J/kg.K)

Definition at line 467 of file TemperaturePressureFunctionFluidProperties.C.

Referenced by cv_from_p_T(), cv_from_v_e(), and e_from_p_T().

 {
   if (_cv_is_constant)
     return _cv;
   else
   {
     Real rho, drho_dp, drho_dT;
     rho_from_p_T(pressure, temperature, rho, drho_dp, drho_dT);
     // Wikipedia notation for thermal expansion / compressibility coefficients
     Real alpha = -drho_dT / rho;
     Real beta = -drho_dp / rho;
     return cp_from_p_T(pressure, temperature) - MathUtils::pow(alpha, 2) * temperature / rho / beta;
   }
 }

◆ cv_from_p_T() [2/2]

void TemperaturePressureFunctionFluidProperties::cv_from_p_T	(	Real	p,
		Real	T,
		Real &	cv,
		Real &	dcv_dp,
		Real &	dcv_dT
	)		const

overridevirtual

Isochoric specific heat capacity and its derivatives from pressure and temperature.

Parameters

[in]	p	pressure (Pa)
[in]	T	temperature (K)
[out]	cv	isochoric specific heat (J/kg/K)
[out]	dcv_dp	derivative of isochoric specific heat w.r.t. pressure (J/kg/K/Pa)

Definition at line 483 of file TemperaturePressureFunctionFluidProperties.C.

 {
   if (_cv_is_constant)
   {
     cv = cv_from_p_T(pressure, temperature);
     dcv_dp = 0.0;
     dcv_dT = 0.0;
   }
   else
   {
     cv = cv_from_p_T(pressure, temperature);
     Real eps = 1e-10;
     Real cv_1p = cv_from_p_T(pressure * (1 + eps), temperature);
     Real cv_1T = cv_from_p_T(pressure, temperature * (1 + eps));
     dcv_dp = (cv_1p - cv) / (pressure * eps);
     dcv_dT = (cv_1T - cv) / (temperature * eps);
   }
 }

◆ cv_from_v_e() [1/2]

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

overridevirtual

Isochoric specific heat from specific volume and specific internal energy.

Parameters

[in]	v	specific volume (m$^3$/kg)
[in]	e	specific internal energy (J/kg)

Returns: isochoric specific heat (J/kg.K)

Definition at line 164 of file TemperaturePressureFunctionFluidProperties.C.

Referenced by cv_from_v_e().

 {
   if (_cv_is_constant)
     return _cv;
   else
   {
     const Real p0 = _p_initial_guess;
     const Real T0 = _T_initial_guess;
     Real p, T;
     bool conversion_succeeded = true;
     p_T_from_v_e(v, e, p0, T0, p, T, conversion_succeeded);
     if (conversion_succeeded)
       return cv_from_p_T(p, T);
     else
       mooseError("cp_from_v_e calculation failed.");
   }
 }

◆ cv_from_v_e() [2/2]

void TemperaturePressureFunctionFluidProperties::cv_from_v_e	(	Real	p,
		Real	T,
		Real &	cv,
		Real &	dcv_dv,
		Real &	dcv_de
	)		const

overridevirtual

Isochoric specific heat capacity and its derivatives from pressure and temperature.

Parameters

[in]	p	pressure (Pa)
[in]	T	temperature (K)
[out]	cv	isochoric specific heat (J/kg/K)
[out]	dcv_dv	derivative of isochoric specific heat w.r.t. specific volume
[out]	dcv_de	derivative of isochoric specific heat w.r.t. specific energy

Definition at line 183 of file TemperaturePressureFunctionFluidProperties.C.

 {
   if (_cv_is_constant)
   {
     cv = cv_from_v_e(v, e);
     dcv_dv = 0.0;
     dcv_de = 0.0;
   }
   else
   {
     const Real p0 = _p_initial_guess;
     const Real T0 = _T_initial_guess;
     Real p, T;
     bool conversion_succeeded = true;
     p_T_from_v_e(v, e, p0, T0, p, T, conversion_succeeded);
     Real dcv_dp, dcv_dT;
     cv_from_p_T(p, T, cv, dcv_dp, dcv_dT);
     if (!conversion_succeeded)
       mooseError("cp_from_v_e and derivatives calculation failed.");
 
     Real p1, T1;
     p_T_from_v_e(v * (1 + 1e-6), e, p0, T0, p1, T1, conversion_succeeded);
     Real dp_dv = (p1 - p) / (v * 1e-6);
     Real dT_dv = (T1 - T) / (v * 1e-6);
     if (!conversion_succeeded)
       mooseError("cp_from_v_e and derivatives calculation failed.");
 
     Real p2, T2;
     p_T_from_v_e(v, e * (1 + 1e-6), p0, T0, p2, T2, conversion_succeeded);
     Real dp_de = (p2 - p) / (e * 1e-6);
     Real dT_de = (T2 - T) / (e * 1e-6);
     if (!conversion_succeeded)
       mooseError("cp_from_v_e and derivatives calculation failed.");
 
     dcv_dv = dcv_dp * dp_dv + dcv_dT * dT_dv;
     dcv_de = dcv_dp * dp_de + dcv_dT * dT_de;
   }
 }

◆ e_from_p_rho()

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

overridevirtual

Specific internal energy from pressure and density.

Parameters

[in]	p	pressure (Pa)
[in]	rho	density (kg/m$^3$)
[out]	e	specific internal energy (J/kg)

Definition at line 401 of file TemperaturePressureFunctionFluidProperties.C.

 {
   if (_cv_is_constant)
   {
     Real temperature = T_from_p_rho(p, rho);
     return _e_ref + _cv * (temperature - _T_ref);
   }
   else
   {
     Real temperature = T_from_p_rho(p, rho);
     return e_from_p_T(p, temperature);
   }
 }

◆ e_from_p_T() [1/2]

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

overridevirtual

Specific internal energy from pressure and temperature.

Parameters

[in]	p	pressure (Pa)
[in]	T	temperature (K)

Returns: specific internal energy (J/kg)

Definition at line 362 of file TemperaturePressureFunctionFluidProperties.C.

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

 {
   if (_cv_is_constant)
     return _e_ref + _cv * (temperature - _T_ref);
   else
   {
     const int n_intervals = std::ceil(std::abs(temperature - _T_ref) / _integration_dT);
     const auto h = (temperature - _T_ref) / n_intervals;
     Real integral = 0;
     // Centered step integration is second-order
     for (const auto i : make_range(n_intervals))
       integral += cv_from_p_T(pressure, _T_ref + (i + 0.5) * h);
     integral *= h;
     // we are still missing the dV or dP term to go from V/P_ref (e_ref = e(T_ref, V/P_ref))
     // to current V. The dT term is the largest one though
     return _e_ref + integral;
   }
 }

◆ e_from_p_T() [2/2]

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

overridevirtual

Specific internal energy and its derivatives from pressure and temperature.

Parameters

[in]	p	pressure (Pa)
[in]	T	temperature (K)
[out]	e	specific internal energy (J/kg)
[out]	de_dp	derivative of specific internal energy w.r.t. pressure
[out]	de_dT	derivative of specific internal energy w.r.t. temperature

Definition at line 382 of file TemperaturePressureFunctionFluidProperties.C.

 {
   if (_cv_is_constant)
   {
     e = e_from_p_T(pressure, temperature);
     de_dp = 0.0;
     de_dT = _cv;
   }
   else
   {
     e = e_from_p_T(pressure, temperature);
     Real ep = e_from_p_T(pressure * (1 + 1e-8), temperature);
     de_dp = (ep - e) / (pressure * 1e-8);
     de_dT = cv_from_p_T(pressure, temperature);
   }
 }

◆ 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 479 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 TemperaturePressureFunctionFluidProperties::fluidName ( ) const

overridevirtual

Fluid name.

Returns: "TemperaturePressureFunctionFluidProperties"

Reimplemented from SinglePhaseFluidProperties.

Definition at line 67 of file TemperaturePressureFunctionFluidProperties.C.

 {
   return "TemperaturePressureFunctionFluidProperties";
 }

◆ h_from_p_T() [1/2]

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

overridevirtual

Specific enthalpy from pressure and temperature.

Parameters

[in]	p	pressure (Pa)
[in]	T	temperature (K)

Returns: specific enthalpy (J/kg)

Definition at line 341 of file TemperaturePressureFunctionFluidProperties.C.

Referenced by T_from_p_h().

 {
   Real e = e_from_p_T(pressure, temperature);
   Real rho = rho_from_p_T(pressure, temperature);
   return e + pressure / rho;
 }

◆ h_from_p_T() [2/2]

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

overridevirtual

Specific enthalpy and its derivatives from pressure and temperature.

Parameters

[in]	p	pressure (Pa)
[in]	T	temperature (K)
[out]	h	specific enthalpy (J/kg)
[out]	dh_dp	derivative of specific enthalpy w.r.t. pressure
[out]	dh_dT	derivative of specific enthalpy w.r.t. temperature

Definition at line 349 of file TemperaturePressureFunctionFluidProperties.C.

 {
   Real e, de_dp, de_dT;
   e_from_p_T(pressure, temperature, e, de_dp, de_dT);
   Real rho, drho_dp, drho_dT;
   rho_from_p_T(pressure, temperature, rho, drho_dp, drho_dT);
   h = e + pressure / rho;
   dh_dp = de_dp + 1. / rho - pressure / rho / rho * drho_dp;
   dh_dT = de_dT - pressure * drho_dT / rho / rho;
 }

◆ 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 374 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 {}

◆ initialSetup()

void TemperaturePressureFunctionFluidProperties::initialSetup ( )

overrideprotectedvirtual

Functions are constructed after fluid properties, so we delay the getting of the Function.

Reimplemented from ThreadedGeneralUserObject.

Definition at line 57 of file TemperaturePressureFunctionFluidProperties.C.

Referenced by cp_from_p_T(), k_from_p_T(), mu_from_p_T(), and rho_from_p_T().

 {
   _k_function = &getFunction("k");
   _rho_function = &getFunction("rho");
   _mu_function = &getFunction("mu");
   _cp_function = isParamValid("cp") ? &getFunction("cp") : nullptr;
   _initialized = true;
 }

◆ k_from_p_T() [1/2]

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

overridevirtual

Thermal conductivity from pressure and temperature.

Parameters

p	pressure (Pa)
T	temperature (K)

Returns: thermal conductivity (W/m.K)

Definition at line 522 of file TemperaturePressureFunctionFluidProperties.C.

Referenced by k_from_p_T(), and k_from_v_e().

 {
   if (!_initialized)
     const_cast<TemperaturePressureFunctionFluidProperties *>(this)->initialSetup();
   return _k_function->value(0, Point(temperature, pressure, 0));
 }

◆ k_from_p_T() [2/2]

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

overridevirtual

Thermal conductivity and its derivatives wrt pressure and temperature.

Parameters

	p	pressure (Pa)
	T	temperature (K)
[out]	k	thermal conductivity (W/m.K)
[out]	dk_dp	derivative of thermal conductivity wrt pressure
[out]	dk_dT	derivative of thermal conductivity wrt temperature

Definition at line 530 of file TemperaturePressureFunctionFluidProperties.C.

 {
   k = k_from_p_T(pressure, temperature);
   const RealVectorValue grad_function = _k_function->gradient(0, Point(temperature, pressure, 0));
   dk_dT = grad_function(0);
   dk_dp = grad_function(1);
 }

◆ k_from_v_e()

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

overridevirtual

Thermal conductivity from specific volume and specific internal energy.

Parameters

[in]	v	specific volume (m$^3$/kg)
[in]	e	specific internal energy (J/kg)

Returns: thermal conductivity (W/m.K)

Definition at line 267 of file TemperaturePressureFunctionFluidProperties.C.

 {
   if (_cv_is_constant)
   {
     Real temperature = T_from_v_e(v, e);
     Real pressure = p_from_v_e(v, e);
     return k_from_p_T(pressure, temperature);
   }
   else
   {
     const Real p0 = _p_initial_guess;
     const Real T0 = _T_initial_guess;
     Real p, T;
     bool conversion_succeeded = true;
     p_T_from_v_e(v, e, p0, T0, p, T, conversion_succeeded);
     if (conversion_succeeded)
       return k_from_p_T(p, T);
     else
       mooseError("k_from_v_e calculation failed.");
   }
 }

◆ 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 476 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 483 of file SinglePhaseFluidProperties.h.

 {
   return {Real{0}, Real{1}};
 }

◆ molarMass()

Real SinglePhaseFluidProperties::molarMass ( ) const

virtualinherited

Molar mass [kg/mol].

Returns: molar mass

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

Definition at line 286 of file SinglePhaseFluidProperties.C.

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

◆ mu_from_p_T() [1/2]

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

overridevirtual

Dynamic viscosity from pressure and temperature.

Parameters

p	pressure (Pa)
T	temperature (K)

Returns: dynamic viscosity (Pa.s)

Definition at line 504 of file TemperaturePressureFunctionFluidProperties.C.

Referenced by mu_from_p_T(), and mu_from_v_e().

 {
   if (!_initialized)
     const_cast<TemperaturePressureFunctionFluidProperties *>(this)->initialSetup();
   return _mu_function->value(0, Point(temperature, pressure, 0));
 }

◆ mu_from_p_T() [2/2]

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

overridevirtual

Dynamic viscosity and its derivatives wrt pressure and temperature.

Parameters

	p	pressure (Pa)
	T	temperature (K)
[out]	mu	viscosity (Pa.s)
[out]	dmu_dp	derivative of viscosity wrt pressure
[out]	dmu_dT	derivative of viscosity wrt temperature

Definition at line 512 of file TemperaturePressureFunctionFluidProperties.C.

 {
   mu = mu_from_p_T(pressure, temperature);
   const RealVectorValue grad_function = _mu_function->gradient(0, Point(temperature, pressure, 0));
   dmu_dT = grad_function(0);
   dmu_dp = grad_function(1);
 }

◆ mu_from_v_e()

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

overridevirtual

Dynamic viscosity from specific volume and specific internal energy.

Parameters

[in]	v	specific volume (m$^3$/kg)
[in]	e	specific internal energy (J/kg)

Returns: dynamic viscosity (Pa.s)

Definition at line 244 of file TemperaturePressureFunctionFluidProperties.C.

 {
   if (_cv_is_constant)
   {
     Real temperature = T_from_v_e(v, e);
     Real pressure = p_from_v_e(v, e);
     return mu_from_p_T(pressure, temperature);
   }
   else
   {
     const Real p0 = _p_initial_guess;
     const Real T0 = _T_initial_guess;
     Real p, T;
     bool conversion_succeeded = true;
     p_T_from_v_e(v, e, p0, T0, p, T, conversion_succeeded);
     if (conversion_succeeded)
       return mu_from_p_T(p, T);
     else
       mooseError("mu_from_v_e calculation failed.");
   }
 }

◆ p_from_v_e()

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

overridevirtual

Pressure from specific volume and specific internal energy.

Parameters

[in]	v	specific volume (m$^3$/kg)
[in]	e	specific internal energy (J/kg)

Returns: pressure (Pa)

Definition at line 224 of file TemperaturePressureFunctionFluidProperties.C.

Referenced by cp_from_v_e(), k_from_v_e(), and mu_from_v_e().

 {
   const Real T = T_from_v_e(v, e);
   // note that p and T inversion in the definition of lambda
   auto lambda = [&](Real T, Real current_p, Real & new_rho, Real & drho_dT, Real & drho_dp)
   { rho_from_p_T(current_p, T, new_rho, drho_dp, drho_dT); };
   Real p = FluidPropertiesUtils::NewtonSolve(
                T, 1. / v, _p_initial_guess, _tolerance, lambda, name() + "::p_from_v_e")
                .first;
   // check for nans
   if (std::isnan(p))
     mooseError("Conversion from specific volume (v = ",
                v,
                ") and specific energy (e = ",
                e,
                ") to pressure failed to converge.");
   return p;
 }

◆ 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 575 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 511 of file SinglePhaseFluidProperties.h.

Referenced by TabulatedBicubicFluidProperties::constructInterpolation(), cp_from_v_e(), cv_from_v_e(), TabulatedFluidProperties::g_from_v_e(), k_from_v_e(), mu_from_v_e(), and 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);
     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 546 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() [1/12]

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 434 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 TemperaturePressureFunctionFluidProperties::rho_from_p_T	(	Real	p,
		Real	T
	)		const

overridevirtual

Density from pressure and temperature.

Parameters

[in]	p	pressure (Pa)
[in]	T	temperature (K)

Returns: density (kg/m$^3$)

Definition at line 290 of file TemperaturePressureFunctionFluidProperties.C.

Referenced by beta_from_p_T(), cp_from_p_T(), cv_from_p_T(), h_from_p_T(), p_from_v_e(), rho_from_p_T(), T_from_p_rho(), and v_from_p_T().

 {
   if (!_initialized)
     const_cast<TemperaturePressureFunctionFluidProperties *>(this)->initialSetup();
   return _rho_function->value(0, Point(temperature, pressure, 0));
 }

◆ rho_from_p_T() [2/3]

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

overridevirtual

Density and its derivatives from pressure and temperature.

Parameters

[in]	p	pressure (Pa)
[in]	T	temperature (K)
[out]	rho	density (kg/m$^3$)
[out]	drho_dp	derivative of density w.r.t. pressure
[out]	drho_dT	derivative of density w.r.t. temperature

Definition at line 298 of file TemperaturePressureFunctionFluidProperties.C.

 {
   rho = rho_from_p_T(pressure, temperature);
   const RealVectorValue grad_function = _rho_function->gradient(0, Point(temperature, pressure, 0));
   drho_dT = grad_function(0);
   drho_dp = grad_function(1);
 }

◆ rho_from_p_T() [3/3]

void TemperaturePressureFunctionFluidProperties::rho_from_p_T	(	const ADReal &	pressure,
		const ADReal &	temperature,
		ADReal &	rho,
		ADReal &	drho_dp,
		ADReal &	drho_dT
	)		const

overridevirtual

Definition at line 308 of file TemperaturePressureFunctionFluidProperties.C.

 {
   rho = rho_from_p_T(pressure, temperature);
   const ADRealVectorValue grad_function =
       _rho_function->gradient(0, Point(temperature.value(), pressure.value(), 0));
   drho_dT = grad_function(0);
   drho_dp = grad_function(1);
 }

◆ 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 448 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 455 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 469 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 TemperaturePressureFunctionFluidProperties::s_from_p_T	(	Real	,
		Real
	)		const

inlineoverride

Definition at line 308 of file TemperaturePressureFunctionFluidProperties.h.

308 { mooseError("Not implemented"); }

ThreadedGeneralUserObject::mooseError

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

◆ s_from_p_T() [2/2]

void TemperaturePressureFunctionFluidProperties::s_from_p_T	(	Real	,
		Real	,
		Real &	,
		Real &	,
		Real &
	)		const

inlineoverride

Definition at line 309 of file TemperaturePressureFunctionFluidProperties.h.

   {
     mooseError("Not implemented");
   }

◆ subdomainSetup()

virtual void FluidProperties::subdomainSetup ( )

inlinefinalvirtualinherited

Reimplemented from ThreadedGeneralUserObject.

Definition at line 38 of file FluidProperties.h.

38 {}

◆ T_from_p_h()

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

overridevirtual

Temperature from pressure and specific enthalpy.

Parameters

[in]	p	pressure (Pa)
[in]	h	specific enthalpy (J/kg)

Returns: temperature (T)

Definition at line 92 of file TemperaturePressureFunctionFluidProperties.C.

 {
   auto lambda = [&](Real p, Real current_T, Real & new_h, Real & dh_dp, Real & dh_dT)
   { h_from_p_T(p, current_T, new_h, dh_dp, dh_dT); };
   Real T = FluidPropertiesUtils::NewtonSolve(
                p, h, _T_initial_guess, _tolerance, lambda, name() + "::T_from_p_h", _max_newton_its)
                .first;
   // check for nans
   if (std::isnan(T))
     mooseError("Conversion from pressure (p = ",
                p,
                ") and enthalpy (h = ",
                h,
                ") to temperature failed to converge.");
   return T;
 }

◆ T_from_p_rho()

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

virtual

Temperature from pressure and density.

Parameters

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

Returns: temperature (T)

Definition at line 110 of file TemperaturePressureFunctionFluidProperties.C.

Referenced by e_from_p_rho().

 {
   auto lambda = [&](Real p, Real current_T, Real & new_rho, Real & drho_dp, Real & drho_dT)
   { rho_from_p_T(p, current_T, new_rho, drho_dp, drho_dT); };
   Real T = FluidPropertiesUtils::NewtonSolve(
                p, rho, _T_initial_guess, _tolerance, lambda, name() + "::T_from_p_rho")
                .first;
   // check for nans
   if (std::isnan(T))
     mooseError("Conversion from pressure (p = ",
                p,
                ") and density (rho = ",
                rho,
                ") to temperature failed to converge.");
   return T;
 }

◆ T_from_v_e()

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

overridevirtual

Temperature from specific volume and specific internal energy.

Parameters

[in]	v	specific volume (m$^3$/kg)
[in]	e	specific internal energy (J/kg)

Returns: temperature (K)

Definition at line 73 of file TemperaturePressureFunctionFluidProperties.C.

Referenced by cp_from_v_e(), k_from_v_e(), mu_from_v_e(), and p_from_v_e().

 {
   if (_cv_is_constant)
     return _T_ref + (e - _e_ref) / _cv;
   else
   {
     const Real p0 = _p_initial_guess;
     const Real T0 = _T_initial_guess;
     Real p, T;
     bool conversion_succeeded = true;
     p_T_from_v_e(v, e, p0, T0, p, T, conversion_succeeded);
     if (conversion_succeeded)
       return T;
     else
       mooseError("T_from_v_e calculation failed.");
   }
 }

◆ 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 322 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 328 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 604 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 624 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 485 of file SinglePhaseFluidProperties.C.

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

◆ v_from_p_T() [1/2]

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

overridevirtual

Specific volume from pressure and temperature.

Parameters

[in]	p	pressure (Pa)
[in]	T	temperature (K)

Returns: specific volume (m$^3$/kg)

Definition at line 322 of file TemperaturePressureFunctionFluidProperties.C.

Referenced by v_from_p_T().

 {
   return 1.0 / rho_from_p_T(pressure, temperature);
 }

◆ v_from_p_T() [2/2]

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

overridevirtual

Specific volume and its derivatives from pressure and temperature.

Parameters

[in]	p	pressure (Pa)
[in]	T	temperature (K)
[out]	v	specific volume (m$^3$/kg)
[out]	dv_dp	derivative of specific volume with respect to pressure
[out]	dv_dT	derivative of specific volume with respect to temperature

Definition at line 328 of file TemperaturePressureFunctionFluidProperties.C.

 {
   v = v_from_p_T(pressure, temperature);
 
   Real rho, drho_dp, drho_dT;
   rho_from_p_T(pressure, temperature, rho, drho_dp, drho_dT);
 
   dv_dp = -v * v * drho_dp;
   dv_dT = -v * v * drho_dT;
 }

◆ validParams()

InputParameters TemperaturePressureFunctionFluidProperties::validParams ( )

static

Definition at line 16 of file TemperaturePressureFunctionFluidProperties.C.

 {
   InputParameters params = SinglePhaseFluidProperties::validParams();
   params.addRequiredParam<FunctionName>(
       "k", "Thermal conductivity function of temperature and pressure [W/(m-K)]");
   params.addRequiredParam<FunctionName>("rho",
                                         "Density function of temperature and pressure [kg/m^3]");
   params.addRequiredParam<FunctionName>(
       "mu", "Dynamic viscosity function of temperature and pressure [Pa-s]");
 
   params.addParam<FunctionName>(
       "cp", "Isobaric specific heat function of temperature and pressure [J/(kg-K)]");
   params.addRangeCheckedParam<Real>(
       "cv", 0, "cv >= 0", "Constant isochoric specific heat [J/(kg-K)]");
   params.addParam<Real>("e_ref", 0, "Specific internal energy at the reference temperature");
   params.addParam<Real>("T_ref", 0, "Reference temperature for the specific internal energy");
   params.addParam<Real>("dT_integration_intervals",
                         10,
                         "Size of intervals for integrating cv(T) to compute e(T) from e(T_ref)");
 
   params.addClassDescription(
       "Single-phase fluid properties that allows to provide thermal "
       "conductivity, density, and viscosity as functions of temperature and pressure.");
   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 368 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 380 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 389 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 404 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 410 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 419 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 490 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];
 }