Class for fluid properties read from a tabulation in a file. More...

#include <TabulatedFluidProperties.h>

Inheritance diagram for TabulatedFluidProperties:

Public Types
typedef DataFileName	DataFileParameterType

Public Member Functions
	TabulatedFluidProperties (const InputParameters &parameters)

virtual void	initialSetup () override

virtual void	constructInterpolation ()=0

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

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

virtual Real	rho_from_p_T (Real pressure, Real temperature) const override

virtual ADReal	rho_from_p_T (const ADReal &pressure, const ADReal &temperature) const override

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

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

virtual Real	rho_from_p_s (Real p, Real s) const override

virtual void	rho_from_p_s (Real p, Real s, Real &rho, Real &drho_dp, Real &drho_ds) const override

virtual Real	v_from_p_T (Real pressure, Real temperature) const override

virtual ADReal	v_from_p_T (const ADReal &pressure, const ADReal &temperature) const override

virtual void	v_from_p_T (Real pressure, Real temperature, Real &v, Real &dv_dp, Real &dv_dT) const override

virtual Real	e_from_p_T (Real pressure, Real temperature) const override

virtual ADReal	e_from_p_T (const ADReal &pressure, const ADReal &temperature) const override

virtual void	e_from_p_T (Real pressure, Real temperature, Real &e, Real &de_dp, Real &de_dT) const override

virtual Real	e_from_p_rho (Real pressure, Real rho) const override

virtual ADReal	e_from_p_rho (const ADReal &pressure, const ADReal &rho) const override

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

virtual Real	T_from_p_rho (Real pressure, Real rho) const

virtual ADReal	T_from_p_rho (const ADReal &pressure, const ADReal &rho) const

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

virtual Real	h_from_p_T (Real p, Real T) const override

virtual ADReal	h_from_p_T (const ADReal &pressure, const ADReal &temperature) const override

virtual void	h_from_p_T (Real pressure, Real temperature, Real &h, Real &dh_dp, Real &dh_dT) const override

virtual Real	mu_from_p_T (Real pressure, Real temperature) const override

virtual void	mu_from_p_T (Real pressure, Real temperature, Real &mu, Real &dmu_dp, Real &dmu_dT) const override

virtual Real	cp_from_p_T (Real pressure, Real temperature) const override

virtual void	cp_from_p_T (Real pressure, Real temperature, Real &cp, Real &dcp_dp, Real &dcp_dT) const override

virtual Real	cv_from_p_T (Real pressure, Real temperature) const override

virtual void	cv_from_p_T (Real pressure, Real temperature, Real &cv, Real &dcv_dp, Real &dcv_dT) const override

virtual Real	c_from_p_T (Real pressure, Real temperature) const override

virtual void	c_from_p_T (Real pressure, Real temperature, Real &c, Real &dc_dp, Real &dc_dT) const override

virtual Real	k_from_p_T (Real pressure, Real temperature) const override

virtual void	k_from_p_T (Real pressure, Real temperature, Real &k, Real &dk_dp, Real &dk_dT) const override

virtual Real	s_from_p_T (Real pressure, Real temperature) const override

virtual void	s_from_p_T (Real p, Real T, Real &s, Real &ds_dp, Real &ds_dT) const override

virtual std::vector< Real >	henryCoefficients () const override
	The following routines are simply forwarded to the 'fp' companion FluidProperties as they are not included in the tabulations presently.

virtual Real	vaporPressure (Real temperature) const override
	Vapor pressure.

virtual void	vaporPressure (Real temperature, Real &psat, Real &dpsat_dT) const override

virtual Real	vaporTemperature (Real pressure) const override
	Vapor temperature.

virtual void	vaporTemperature (Real pressure, Real &Tsat, Real &dTsat_dp) const override

virtual Real	T_from_p_h (Real pressure, Real enthalpy) const override

virtual ADReal	T_from_p_h (const ADReal &pressure, const ADReal &enthalpy) const override

virtual Real	triplePointPressure () const override
	Triple point pressure.

virtual Real	triplePointTemperature () const override
	Triple point temperature.

virtual Real	criticalPressure () const override
	Critical pressure.

virtual Real	criticalTemperature () const override
	Critical temperature.

virtual Real	criticalDensity () const override
	Critical density.

virtual Real	p_from_v_e (Real v, Real e) const override
	Derivatives like dc_dv & dc_de are computed using the chain rule dy/dx(p,T) = dy/dp * dp/dx + dy/dT * dT/dx where y = c, cp, cv... & x = v, e.

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

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

virtual Real	T_from_v_e (Real v, Real e) const override

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

virtual void	T_from_v_e (const ADReal &v, const ADReal &e, ADReal &p, ADReal &dp_dv, ADReal &dp_de) const override

virtual Real	c_from_v_e (Real v, Real e) const override

virtual void	c_from_v_e (Real v, Real e, Real &c, Real &dc_dv, Real &dc_de) const override

virtual Real	cp_from_v_e (Real v, Real e) const override

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

virtual Real	cv_from_v_e (Real v, Real e) const override

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

virtual Real	mu_from_v_e (Real v, Real e) const override

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

virtual Real	k_from_v_e (Real v, Real e) const override

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

virtual Real	g_from_v_e (Real v, Real e) const override

virtual Real	e_from_v_h (Real v, Real h) const override

virtual void	e_from_v_h (Real v, Real h, Real &e, Real &de_dv, Real &de_dh) const override

virtual Real	T_from_h_s (Real h, Real s) const

virtual Real	T_from_p_s (Real p, Real s) const

virtual void	T_from_p_s (Real p, Real s, Real &T, Real &dT_dp, Real &dT_ds) const

virtual Real	s_from_v_e (Real v, Real e) const override

virtual void	s_from_v_e (Real v, Real e, Real &s, Real &ds_dv, Real &ds_de) const override

virtual Real	s_from_h_p (Real h, Real pressure) const override

virtual void	s_from_h_p (Real h, Real pressure, Real &s, Real &ds_dh, Real &ds_dp) const override

virtual Real	criticalInternalEnergy () const
	Critical specific internal energy.

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

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

virtual ADReal	vaporPressure (const ADReal &T) const

virtual ADReal	vaporTemperature (const ADReal &p) const

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

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

virtual void	rho_mu_from_p_T (Real p, Real T, Real &rho, Real &mu) const
	Combined methods.

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.

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.

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.

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	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	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)

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 Types
enum	OOBBehavior { Ignore , Throw , DeclareInvalid , WarnInvalid , SetToClosestBound }
	Enum specifying all the behavior on out of bounds data options. More...

Protected Member Functions
void	writeTabulatedData (std::string file_name)
	Writes tabulated data to a file.

template<typename T >
void	checkInputVariables (T &pressure, T &temperature) const
	Checks that the inputs are within the range of the tabulated data, and throws an error if they are not.

template<typename T >
void	checkInputVariablesVE (T &v, T &e) const
	Checks that the inputs are within the range of the tabulated data, and throws an error if they are not.

virtual void	checkInitialGuess (bool post_reading_tabulation) const
	Checks initial guess for Newton Method.

void	readFileTabulationData (bool use_pT)
	Read tabulation data from file.

void	checkFileTabulationGrids (std::vector< Real > &v1, std::vector< Real > &v2, const std::string &file_name, const std::string &v1_name, const std::string &v2_name)
	Check that the tabulation grids in the file are correct (no repeats etc)

virtual void	generateTabulatedData ()
	Generates a table of fluid properties by looping over pressure and temperature and calculating properties using the FluidProperties UserObject _fp.

virtual void	generateVETabulatedData ()
	Generates a table of fluid properties by looping over specific volume and internal energy and calculating properties using the FluidProperties UserObject _fp.

void	computePropertyIndicesInInterpolationVectors ()
	Retrieves the index for each property in the vector of interpolations.

void	createVGridVector ()
	Create (or reset) the grid vectors for the specific volume and internal energy interpolations The order of priority for determining the range boundaries in v and e:

void	createVEGridVectors ()

void	createVHGridVectors ()
	Create (or reset) the grid vectors for the specific volume and enthalpy interpolation The order of priority for determining the range boundaries in v and h:

void	missingVEInterpolationError (const std::string &function_name) const
	Standardized error message for missing interpolation.

void	TabulationNotImplementedError (const std::string &desired_routine) const
	Utility to forward errors related to fluid properties methods not implemented.

void	NeedTabulationOrFPError (const std::string &desired_routine, const std::string &needed_property) const
	Utility to forward errors related to fluid properties needing more data for their computation This should generally be used as an 'else' condition to if (_interpolate_property) / else if (_fp)

void	NeedTabulationError (const std::string &needed_property) const
	Utility to forward errors related to properties being requested for tabulation, but no tabulation is present This should generally be used as an 'else' condition to if (_interpolate_needed_property)

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.

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)

static std::string	meshPropertyName (const std::string &data_name, const std::string &prefix)

Protected Attributes
FileName	_file_name_in
	File name of input tabulated data file.

FileName	_file_name_ve_in
	File name of input (v,e) tabulated data file.

FileName	_file_name_out
	File name of output tabulated data file.

FileName	_file_name_ve_out
	File name of output (v,e) tabulated data file.

const bool	_save_file
	Whether to save a generated fluid properties file to disk.

std::vector< Real >	_pressure
	Pressure vector.

std::vector< Real >	_temperature
	Temperature vector.

std::vector< Real >	_specific_volume
	Specific volume vector.

std::vector< Real >	_internal_energy
	Specific internal energy vector.

std::vector< Real >	_enthalpy
	Specific enthalpy vector.

const bool	_create_direct_pT_interpolations
	Whether the object has direct (p,T) interpolations (whether created from file or from _fp)

const bool	_create_direct_ve_interpolations
	Whether the object has direct (v,e) interpolations (whether created from file or from _fp)

std::vector< std::vector< Real > >	_properties
	Tabulated fluid properties (read from file OR computed from _fp)

std::vector< std::vector< Real > >	_properties_ve
	Tabulated fluid properties in (v,e) (read from file OR computed from _fp)

std::vector< std::unique_ptr< BidimensionalInterpolation > >	_property_ipol
	Vector of bi-dimensional interpolation of fluid properties.

std::vector< std::unique_ptr< BidimensionalInterpolation > >	_property_ve_ipol
	Vector of bi-dimensional interpolation of fluid properties directly in (v,e)

Real	_temperature_min
	Minimum temperature in tabulated data.

Real	_temperature_max
	Maximum temperature in tabulated data.

Real	_pressure_min
	Minimum pressure in tabulated data.

Real	_pressure_max
	Maximum pressure in tabulated data.

unsigned int	_num_T
	Number of temperature points in the tabulated data.

unsigned int	_num_p
	Number of pressure points in the tabulated data.

const SinglePhaseFluidProperties *const	_fp
	SinglePhaseFluidPropertiesPT UserObject.

const bool	_allow_fp_and_tabulation
	Whether to allow a fp object when a tabulation is in use.

MultiMooseEnum	_interpolated_properties_enum
	Properties to be interpolated entered in the input file.

std::vector< std::string >	_interpolated_properties
	List of properties to be interpolated.

bool	_interpolate_density
	Set of flags to note whether a property is to be interpolated.

bool	_interpolate_enthalpy

bool	_interpolate_internal_energy

bool	_interpolate_viscosity

bool	_interpolate_k

bool	_interpolate_c

bool	_interpolate_cp

bool	_interpolate_cv

bool	_interpolate_entropy

bool	_interpolate_pressure

bool	_interpolate_temperature

unsigned int	_density_idx
	Index of each property.

unsigned int	_enthalpy_idx

unsigned int	_internal_energy_idx

unsigned int	_viscosity_idx

unsigned int	_k_idx

unsigned int	_c_idx

unsigned int	_cp_idx

unsigned int	_cv_idx

unsigned int	_entropy_idx

unsigned int	_p_idx

unsigned int	_T_idx

MooseUtils::DelimitedFileReader	_csv_reader
	The MOOSE delimited file reader.

bool	_construct_pT_from_ve
	if the lookup table p(v, e) and T(v, e) should be constructed

bool	_construct_pT_from_vh
	if the lookup table p(v, h) and T(v, h) should be constructed

bool	_initial_setup_done
	keeps track of whether initialSetup has been performed

unsigned int	_num_v
	Number of specific volume points in the tabulated data.

unsigned int	_num_e
	Number of internal energy points in tabulated data.

bool	_log_space_v
	log-space the specific volume interpolation grid axis instead of linear

bool	_log_space_e
	log-space the internal energy interpolation grid axis instead of linear

bool	_log_space_h
	log-space the enthalpy interpolation grid axis instead of linear

MooseEnum	_OOBBehavior
	User-selected out-of-bounds behavior.

std::unique_ptr< BidimensionalInterpolation >	_T_from_v_e_ipol
	Bi-dimensional interpolation of temperature from (v,e)

std::unique_ptr< BidimensionalInterpolation >	_p_from_v_e_ipol
	Bi-dimensional interpolation of pressure from (v,e)

std::unique_ptr< BidimensionalInterpolation >	_T_from_v_h_ipol
	Bi-dimensional interpolation of temperature from (v,h)

std::unique_ptr< BidimensionalInterpolation >	_p_from_v_h_ipol
	Bidimensional interpolation of pressure from (v,h)

bool	_e_bounds_specified
	Whether the specific internal energy bounds were set by the user.

bool	_v_bounds_specified
	Whether the specific volume bounds were set by the user.

Real	_e_min
	Minimum internal energy in tabulated data (can be user-specified)

Real	_e_max
	Maximum internal energy in tabulated data (can be user-specified)

Real	_v_min
	Minimum specific volume in tabulated data (can be user-specified)

Real	_v_max
	Maximum specific volume in tabulated data (can be user-specified)

Real	_h_min
	Minimum specific enthalpy in tabulated data.

Real	_h_max
	Maximum specific enthalpy in tabulated data.

const Real	_tolerance
	Newton's method may be used to convert between variable sets.

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

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

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

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

const Real	_T_c2k
	Conversion of temperature from Celsius to Kelvin.

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

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

Private Member Functions
void	unimplementedDerivativeMethod (const std::string &property_function_name) const

const Moose::FunctionBase *	getKokkosFunctionByNameHelper (const FunctionName &name) const

const UserObjectBase &	getUserObjectFromFEProblem (const UserObjectName &object_name, const THREAD_ID tid=0) const

const T &	castUserObject (const UserObjectBase &uo_base, const std::string &param_name="") const

void	mooseObjectError (const std::string &param_name, std::stringstream &oss) const

const std::string &	userObjectType (const UserObjectBase &uo) const

const std::string &	userObjectName (const UserObjectBase &uo) const

const PostprocessorName &	getPostprocessorNameInternal (const std::string &param_name, const unsigned int index, const bool allow_default_value=true) const

bool	isDefaultPostprocessorValueByName (const PostprocessorName &name) const

PostprocessorValue	getDefaultPostprocessorValueByName (const PostprocessorName &name) const

void	checkParam (const std::string &param_name, const unsigned int index=std::numeric_limits< unsigned int >::max()) const

bool	postprocessorsAdded () const

const VectorPostprocessorValue &	getVectorPostprocessorByNameHelper (const VectorPostprocessorName &name, const std::string &vector_name, bool broadcast, std::size_t t_index) const

const VectorPostprocessorContext< VectorPostprocessorValue > &	getVectorPostprocessorContextByNameHelper (const VectorPostprocessorName &name, const std::string &vector_name) const

bool	vectorPostprocessorsAdded () const

bool	reportersAdded () const

void	possiblyCheckHasReporter (const ReporterName &reporter_name, const std::string &param_name="") const

RestartableDataValue &	registerRestartableDataOnApp (std::unique_ptr< RestartableDataValue > data, THREAD_ID tid) const

void	registerRestartableNameWithFilterOnApp (const std::string &name, Moose::RESTARTABLE_FILTER filter)

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

virtual std::string	meshPropertyPrefix (const std::string &data_name) const

const RestartableDataValue &	getMeshPropertyInternal (const std::string &data_name, const std::string &prefix) const

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

const VariableValue *	getDefaultValue (const std::string &var_name) const

const ADVariableValue *	getADDefaultValue (const std::string &var_name) const

void	checkVar (const std::string &var_name) const

void	validateExecutionerType (const std::string &name, const std::string &fn_name) const

Moose::MaterialDataType	getMaterialDataType (const std::set< BoundaryID > &boundary_ids) const

unsigned int	getMaxQps () const

void	addConsumedPropertyName (const MooseObjectName &obj_name, const std::string &prop_name)

const PostprocessorValue &	getPostprocessorValueInternal (const std::string &param_name, unsigned int index, std::size_t t_index) const

const PostprocessorValue &	getPostprocessorValueInternal (const std::string &param_name, unsigned int index, std::size_t t_index) const

const PostprocessorValue &	getPostprocessorValueByNameInternal (const PostprocessorName &name, std::size_t t_index) const

const PostprocessorValue &	getPostprocessorValueByNameInternal (const PostprocessorName &name, std::size_t t_index) const

void	possiblyCheckHasVectorPostprocessor (const std::string &param_name, const std::string &vector_name) const

void	possiblyCheckHasVectorPostprocessor (const std::string &param_name, const std::string &vector_name) const

void	possiblyCheckHasVectorPostprocessorByName (const VectorPostprocessorName &name, const std::string &vector_name) const

void	possiblyCheckHasVectorPostprocessorByName (const VectorPostprocessorName &name, const std::string &vector_name) const

Static Private Member Functions
static const hit::Node *	getHitNode (const InputParameters &params)

static std::string	messagePrefix (const InputParameters &params, const bool hit_prefix)

Private Attributes
UserObject *	_primary_thread_copy

std::set< std::string >	_supplied_uo

const ParallelParamObject &	_parent

const MooseBase &	_si_moose_base

const FEProblemBase *	_si_problem

ExecFlagEnum	_empty_execute_enum

const MooseObject &	_fni_object

const InputParameters &	_fni_params

FEProblemBase &	_fni_feproblem

const THREAD_ID	_fni_tid

const MooseObject &	_uoi_moose_object

const FEProblemBase &	_uoi_feproblem

const THREAD_ID	_uoi_tid

const MooseObject &	_ppi_moose_object

const InputParameters &	_ppi_params

const FEProblemBase &	_ppi_feproblem

std::map< PostprocessorName, std::unique_ptr< PostprocessorValue > >	_default_values

const bool	_broadcast_by_default

const MooseObject &	_vpi_moose_object

const FEProblemBase &	_vpi_feproblem

const THREAD_ID	_vpi_tid

const InputParameters &	_ri_params

FEProblemBase &	_ri_fe_problem_base

const ReporterData &	_ri_reporter_data

const MooseObject &	_ri_moose_object

const InputParameters &	_dni_params

FEProblemBase &	_dni_feproblem

const MooseObject *const	_dni_moose_object_ptr

const InputParameters &	_si_params

FEProblemBase &	_si_feproblem

THREAD_ID	_si_tid

const RestartableDataMapName	_metaname

std::string	_restartable_name

MooseApp &	_meta_data_app

const MooseObject *const	_meta_data_object

const InputParameters &	_sc_parameters

const std::string &	_sc_name

const bool	_sc_is_implicit

std::unordered_map< std::string, std::vector< MooseVariableScalar * > >	_coupled_scalar_vars

std::unordered_map< std::string, std::unique_ptr< VariableValue > >	_default_value

std::unordered_map< std::string, std::unique_ptr< ADVariableValue > >	_dual_default_value

std::vector< MooseVariableScalar * >	_coupled_moose_scalar_vars

std::unordered_map< std::string, std::vector< MooseVariableFieldBase * > >	_sc_coupled_vars

std::set< TagID >	_sc_coupleable_vector_tags

std::set< TagID >	_sc_coupleable_matrix_tags

const MooseObject &	_mi_moose_object

const bool	_mi_boundary_restricted

const std::set< SubdomainID > &	_mi_block_ids

const std::set< BoundaryID > &	_mi_boundary_ids

std::vector< std::unique_ptr< OptionalMaterialPropertyProxyBase< MaterialPropertyInterface > > >	_optional_property_proxies

const std::string	_ti_name

	propfunc (p, v, e) propfunc(T
	Compute a fluid property given for the state defined by two given properties.

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

Class for fluid properties read from a tabulation in a file.

Definition at line 26 of file TabulatedFluidProperties.h.

Member Enumeration Documentation

◆ OOBBehavior

enum TabulatedFluidProperties::OOBBehavior

protected

Enum specifying all the behavior on out of bounds data options.

Enumerator
Ignore
Throw
DeclareInvalid
WarnInvalid
SetToClosestBound

Definition at line 383 of file TabulatedFluidProperties.h.

  {
    Ignore,
    Throw,
    DeclareInvalid,
    WarnInvalid,
    SetToClosestBound
  };

Constructor & Destructor Documentation

◆ TabulatedFluidProperties()

TabulatedFluidProperties::TabulatedFluidProperties ( const InputParameters & parameters )

Definition at line 163 of file TabulatedFluidProperties.C.

  : SinglePhaseFluidProperties(parameters),
    _file_name_in(isParamValid("fluid_property_file") ? getParam<FileName>("fluid_property_file")
                                                      : ""),
    _file_name_ve_in(
        isParamValid("fluid_property_ve_file") ? getParam<FileName>("fluid_property_ve_file") : ""),
    _file_name_out(isParamValid("fluid_property_output_file")
                       ? getParam<FileName>("fluid_property_output_file")
                       : ""),
    _file_name_ve_out(isParamValid("fluid_property_ve_output_file")
                          ? getParam<FileName>("fluid_property_ve_output_file")
                          : ""),
    _save_file(isParamValid("save_file") ? getParam<bool>("save_file")
                                         : (isParamValid("fluid_property_output_file") ||
                                            isParamValid("fluid_property_ve_output_file"))),
    _create_direct_pT_interpolations(getParam<bool>("create_pT_interpolations")),
    _create_direct_ve_interpolations(getParam<bool>("create_ve_interpolations")),
    _temperature_min(getParam<Real>("temperature_min")),
    _temperature_max(getParam<Real>("temperature_max")),
    _pressure_min(getParam<Real>("pressure_min")),
    _pressure_max(getParam<Real>("pressure_max")),
    _num_T(getParam<unsigned int>("num_T")),
    _num_p(getParam<unsigned int>("num_p")),
    // work-around to allow use of 'fp' in GlobalParams
    _fp(isParamValid("input_fp") ? ((getParam<UserObjectName>("input_fp") != name())
                                        ? &getUserObject<SinglePhaseFluidProperties>("input_fp")
                                        : nullptr)
                                 : nullptr),
    _allow_fp_and_tabulation(getParam<bool>("allow_fp_and_tabulation")),
    _interpolated_properties_enum(getParam<MultiMooseEnum>("interpolated_properties")),
    _interpolated_properties(),
    _interpolate_density(false),
    _interpolate_enthalpy(false),
    _interpolate_internal_energy(false),
    _interpolate_viscosity(false),
    _interpolate_k(false),
    _interpolate_c(false),
    _interpolate_cp(false),
    _interpolate_cv(false),
    _interpolate_entropy(false),
    _interpolate_pressure(false),
    _interpolate_temperature(false),
    _density_idx(libMesh::invalid_uint),
    _enthalpy_idx(libMesh::invalid_uint),
    _internal_energy_idx(libMesh::invalid_uint),
    _viscosity_idx(libMesh::invalid_uint),
    _k_idx(libMesh::invalid_uint),
    _c_idx(libMesh::invalid_uint),
    _cp_idx(libMesh::invalid_uint),
    _cv_idx(libMesh::invalid_uint),
    _entropy_idx(libMesh::invalid_uint),
    _p_idx(libMesh::invalid_uint),
    _T_idx(libMesh::invalid_uint),
    _csv_reader(_file_name_in, &_communicator),
    _construct_pT_from_ve(getParam<bool>("construct_pT_from_ve")),
    _construct_pT_from_vh(getParam<bool>("construct_pT_from_vh")),
    _initial_setup_done(false),
    _num_v(getParam<unsigned int>("num_v")),
    _num_e(getParam<unsigned int>("num_e")),
    _log_space_v(getParam<bool>("use_log_grid_v")),
    _log_space_e(getParam<bool>("use_log_grid_e")),
    _log_space_h(getParam<bool>("use_log_grid_h")),
    _OOBBehavior(getParam<MooseEnum>("out_of_bounds_behavior")),
    _e_min(0),
    _e_max(0),
    _v_min(0),
    _v_max(0)
{
  // Check that initial guess (used in Newton Method) is within min and max values
  checkInitialGuess(false);
  // Sanity check on minimum and maximum temperatures and pressures
  if (_temperature_max <= _temperature_min)
    mooseError("temperature_max must be greater than temperature_min");
  if (_pressure_max <= _pressure_min)
    mooseError("pressure_max must be greater than pressure_min");
 
  // Set (v,e) bounds if specified by the user
  if (isParamValid("e_min") && isParamValid("e_max"))
  {
    _e_min = getParam<Real>("e_min");
    _e_max = getParam<Real>("e_max");
    _e_bounds_specified = true;
  }
  else if (isParamValid("e_min") || isParamValid("e_max"))
    paramError("e_min",
               "Either both or none of the min and max values of the specific internal energy "
               "should be specified");
  else
    _e_bounds_specified = false;
  if (isParamValid("v_min") && isParamValid("v_max"))
  {
    _v_min = getParam<Real>("v_min");
    _v_max = getParam<Real>("v_max");
    _v_bounds_specified = true;
  }
  else if (isParamValid("v_min") || isParamValid("v_max"))
    paramError("v_min",
               "Either both or none of the min and max values of the specific volume "
               "should be specified");
  else
    _v_bounds_specified = false;
 
  // Handle out of bounds behavior parameters and deprecation
  if (isParamValid("error_on_out_of_bounds") && getParam<bool>("error_on_out_of_bounds") &&
      _OOBBehavior != Throw)
    paramError("out_of_bounds_behavior", "Inconsistent selection of out of bounds behavior.");
  else if (isParamValid("error_on_out_of_bounds") && !getParam<bool>("error_on_out_of_bounds"))
    _OOBBehavior = SetToClosestBound;
 
  // Lines starting with # in the data file are treated as comments
  _csv_reader.setComment("#");
 
  // Can only and must receive one source of data between fp and tabulations
  if (_fp && (!_file_name_in.empty() || !_file_name_ve_in.empty()) && !_allow_fp_and_tabulation)
    paramError(
        "fluid_property_file",
        "Cannot supply both a fluid properties object with 'input_fp' and a source tabulation "
        "file with 'fluid_property_file', unless 'allow_fp_and_tabulation' is set to true");
  if (!_fp && _file_name_in.empty() && _file_name_ve_in.empty())
    paramError(
        "fluid_property_file",
        "Either a fluid properties object with the parameter 'input_fp' and a source tabulation "
        "file with the parameter 'fluid_property_file' or 'fluid_property_ve_file' should "
        "be provided.");
  if (!_create_direct_pT_interpolations && !_create_direct_ve_interpolations)
    paramError("create_pT_interpolations", "Must create either (p,T) or (v,e) interpolations");
 
  // Some parameters are not used when reading a tabulation
  if (!_fp && !_file_name_in.empty() &&
      (isParamSetByUser("pressure_min") || isParamSetByUser("pressure_max") ||
       isParamSetByUser("temperature_min") || isParamSetByUser("temperature_max")))
    mooseWarning("User-specified bounds in pressure and temperature are ignored when reading a "
                 "'fluid_property_file'. The tabulation bounds are selected "
                 "from the bounds of the input tabulation.");
  if (!_fp && !_file_name_in.empty() && (isParamSetByUser("num_p") || isParamSetByUser("num_T")))
    mooseWarning("User-specified grid sizes in pressure and temperature are ignored when reading a "
                 "'fluid_property_file'. The tabulation bounds are selected "
                 "from the bounds of the input tabulation.");
  if (!_fp && !_file_name_ve_in.empty() &&
      (isParamSetByUser("v_min") || isParamSetByUser("v_max") || isParamSetByUser("e_min") ||
       isParamSetByUser("e_max")))
    mooseWarning(
        "User-specified bounds in specific volume and internal energy are ignored when reading a "
        "'fluid_property_ve_file'. The tabulation bounds are selected "
        "from the bounds of the input tabulation.");
  if (!_fp && !_file_name_ve_in.empty() && (isParamSetByUser("num_e") || isParamSetByUser("num_v")))
    mooseWarning("User-specified grid sizes in specific volume and internal energy are ignored "
                 "when reading a 'fluid_property_ve_file'. The tabulation widths are read "
                 "from the input tabulation.");
  if (!_file_name_ve_in.empty() && (_log_space_v || _log_space_e))
    mooseWarning(
        "User specfied logarithmic grids in specific volume and energy are ignored when reading a "
        "'fluid_properties_ve_file'. The tabulation grid is read from the input tabulation");
}

Member Function Documentation

◆ c_from_p_T() [1/2]

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

overridevirtual

Definition at line 1022 of file TabulatedFluidProperties.C.

{
  if (_interpolate_c && _create_direct_pT_interpolations)
  {
    checkInputVariables(pressure, temperature);
    return _property_ipol[_c_idx]->sample(pressure, temperature);
  }
  else
  {
    if (_fp)
      return _fp->c_from_p_T(pressure, temperature);
    else
      NeedTabulationOrFPError("c_from_p_T", "c");
  }
}

Referenced by c_from_v_e(), and c_from_v_e().

◆ c_from_p_T() [2/2]

void TabulatedFluidProperties::c_from_p_T	(	Real	pressure,
		Real	temperature,
		Real &	c,
		Real &	dc_dp,
		Real &	dc_dT
	)		const

overridevirtual

Definition at line 1039 of file TabulatedFluidProperties.C.

{
  if (_interpolate_c && _create_direct_pT_interpolations)
  {
    checkInputVariables(pressure, temperature);
    _property_ipol[_c_idx]->sampleValueAndDerivatives(pressure, temperature, c, dc_dp, dc_dT);
  }
  else
  {
    if (_fp)
      _fp->c_from_p_T(pressure, temperature, c, dc_dp, dc_dT);
    else
      NeedTabulationOrFPError("c_from_p_T with derivatives", "c");
  }
}

◆ c_from_v_e() [1/2]

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

overridevirtual

Definition at line 1481 of file TabulatedFluidProperties.C.

{
  if (_interpolate_c && !_construct_pT_from_ve && !_create_direct_ve_interpolations)
    missingVEInterpolationError(__PRETTY_FUNCTION__);
  checkInputVariablesVE(v, e);
 
  if (_create_direct_ve_interpolations && _interpolate_c)
    return _property_ve_ipol[_c_idx]->sample(v, e);
  else if (_construct_pT_from_ve)
  {
    Real p = _p_from_v_e_ipol->sample(v, e);
    Real T = _T_from_v_e_ipol->sample(v, e);
    return c_from_p_T(p, T);
  }
  else if (_fp)
    return _fp->c_from_v_e(v, e);
  else
    NeedTabulationOrFPError("c_from_v_e", "c");
}

Referenced by writeTabulatedData().

◆ c_from_v_e() [2/2]

void TabulatedFluidProperties::c_from_v_e	(	Real	v,
		Real	e,
		Real &	c,
		Real &	dc_dv,
		Real &	dc_de
	)		const

overridevirtual

Definition at line 1502 of file TabulatedFluidProperties.C.

{
  if (_interpolate_c && !_construct_pT_from_ve && !_create_direct_ve_interpolations)
    missingVEInterpolationError(__PRETTY_FUNCTION__);
  checkInputVariablesVE(v, e);
 
  if (_create_direct_ve_interpolations && _interpolate_c)
    _property_ve_ipol[_c_idx]->sampleValueAndDerivatives(v, e, c, dc_dv, dc_de);
  else if (_construct_pT_from_ve)
  {
    Real p, dp_dv, dp_de;
    _p_from_v_e_ipol->sampleValueAndDerivatives(v, e, p, dp_dv, dp_de);
    Real T, dT_dv, dT_de;
    _T_from_v_e_ipol->sampleValueAndDerivatives(v, e, T, dT_dv, dT_de);
    Real dc_dp, dc_dT;
    c_from_p_T(p, T, c, dc_dp, dc_dT);
    dc_dv = dc_dp * dp_dv + dc_dT * dT_dv;
    dc_de = dc_dp * dp_de + dc_dT * dT_de;
  }
  else if (_fp)
    _fp->c_from_v_e(v, e, c, dc_dv, dc_de);
  else
    NeedTabulationOrFPError("c_from_v_e with derivatives", "c");
}

◆ checkFileTabulationGrids()

void TabulatedFluidProperties::checkFileTabulationGrids	(	std::vector< Real > &	v1,
		std::vector< Real > &	v2,
		const std::string &	file_name,
		const std::string &	v1_name,
		const std::string &	v2_name
	)

protected

Check that the tabulation grids in the file are correct (no repeats etc)

Parameters

v1	the first grid axis (pressure for pT grid)
v2	the second grid axis (temperature for pT grid)
file_name	the name of the tabulation file

Definition at line 2499 of file TabulatedFluidProperties.C.

{
  // NOTE: We kept the comments in terms of pressure & temperature for clarity
  // Pressure (v1) and temperature (v2) data contains duplicates due to the csv format.
  // First, check that pressure (v1) is monotonically increasing
  if (!std::is_sorted(v1.begin(), v1.end()))
    mooseError("The column data for ", v1_name, " is not monotonically increasing in ", file_name);
 
  // The first pressure (v1) value is repeated for each temperature (v2) value. Counting the
  // number of repeats provides the number of temperature (v2) values
  auto num_v2 = std::count(v1.begin(), v1.end(), v1.front());
 
  // Now remove the duplicates in the pressure (v1) vector
  auto last_unique = std::unique(v1.begin(), v1.end());
  v1.erase(last_unique, v1.end());
 
  // Check that the number of rows in the csv file is equal to _num_v1 * _num_v2
  // v2 is currently the same size as the column_data (will get trimmed at the end)
  if (v2.size() != v1.size() * libMesh::cast_int<unsigned int>(num_v2))
    mooseError("The number of rows in ",
               file_name,
               " is not equal to the number of unique ",
               v1_name,
               " values ",
               v1.size(),
               " multiplied by the number of unique ",
               v2_name,
               " values ",
               num_v2);
 
  // Need to make sure that the temperature (v2) values are provided in ascending order
  std::vector<Real> base_v2(v2.begin(), v2.begin() + num_v2);
  if (!std::is_sorted(base_v2.begin(), base_v2.end()))
    mooseError("The column data for ", v2_name, " is not monotonically increasing in ", file_name);
 
  // Need to make sure that the temperature (v2) are repeated for each pressure (v1) grid point
  auto it_v2 = v2.begin() + num_v2;
  for (const auto i : make_range(v1.size() - 1))
  {
    std::vector<Real> repeated_v2(it_v2, it_v2 + num_v2);
    if (repeated_v2 != base_v2)
      mooseError(v2_name,
                 " values for ",
                 v1_name,
                 " ",
                 v1[i + 1],
                 " are not identical to values for ",
                 v1[0]);
 
    std::advance(it_v2, num_v2);
  }
 
  // At this point, all temperature (v2) data has been provided in ascending order
  // identically for each pressure (v1) value, so we can just keep the first range
  v2.erase(v2.begin() + num_v2, v2.end());
}

Referenced by readFileTabulationData().

◆ checkInitialGuess()

void TabulatedFluidProperties::checkInitialGuess ( bool post_reading_tabulation ) const

protectedvirtual

Checks initial guess for Newton Method.

Parameters

post_reading_tabulation whether the check is performed at construction (false) or after reading a file tabulation (true)

Definition at line 2308 of file TabulatedFluidProperties.C.

{
  // First condition applies when generating a tabulation
  // Second condition applies when using a pre-generated loaded tabulation
  if ((!post_reading_tabulation && _fp && (_construct_pT_from_ve || _construct_pT_from_vh)) ||
      (post_reading_tabulation && (_file_name_in != "" || _file_name_ve_in != "") &&
       (_create_direct_ve_interpolations || isParamSetByUser("T_initial_guess") ||
        isParamSetByUser("p_initial_guess"))))
  {
    if (_p_initial_guess < _pressure_min || _p_initial_guess > _pressure_max)
      mooseWarning("Pressure initial guess for (p,T), (v,e) conversions " +
                   Moose::stringify(_p_initial_guess) +
                   " is outside the range of tabulated "
                   "pressure (" +
                   Moose::stringify(_pressure_min) + ", " + Moose::stringify(_pressure_max) + ").");
 
    if (_T_initial_guess < _temperature_min || _T_initial_guess > _temperature_max)
      mooseWarning("Temperature initial guess for (p,T), (v,e) conversions " +
                   Moose::stringify(_T_initial_guess) +
                   " is outside the range of tabulated "
                   "temperature (" +
                   Moose::stringify(_temperature_min) + ", " + Moose::stringify(_temperature_max) +
                   ").");
  }
}

Referenced by readFileTabulationData(), and TabulatedFluidProperties().

◆ checkInputVariables()

template<typename T >

template void TabulatedFluidProperties::checkInputVariables	(	T &	pressure,
		T &	temperature
	)		const

protected

Checks that the inputs are within the range of the tabulated data, and throws an error if they are not.

Parameters

pressure	input pressure (Pa)
temperature	input temperature (K)

Definition at line 2222 of file TabulatedFluidProperties.C.

{
  using std::max, std::min;
 
  if (_OOBBehavior == Ignore)
    return;
  else if (MooseUtils::absoluteFuzzyGreaterThan(_pressure_min, pressure, libMesh::TOLERANCE) ||
           MooseUtils::absoluteFuzzyGreaterThan(pressure, _pressure_max, libMesh::TOLERANCE))
  {
    if (_OOBBehavior == Throw)
      throw MooseException("Pressure " + Moose::stringify(pressure) +
                           " is outside the range of tabulated pressure (" +
                           Moose::stringify(_pressure_min) + ", " +
                           Moose::stringify(_pressure_max) + ").");
 
    else
    {
      pressure = max(_pressure_min, min(pressure, _pressure_max));
      if (_OOBBehavior == DeclareInvalid)
        flagInvalidSolution("Pressure out of bounds");
      else if (_OOBBehavior == WarnInvalid)
        flagSolutionWarning("Pressure out of bounds");
    }
  }
 
  if (MooseUtils::absoluteFuzzyGreaterThan(_temperature_min, temperature, libMesh::TOLERANCE) ||
      MooseUtils::absoluteFuzzyGreaterThan(temperature, _temperature_max, libMesh::TOLERANCE))
  {
    if (_OOBBehavior == Throw)
      throw MooseException("Temperature " + Moose::stringify(temperature) +
                           " is outside the range of tabulated temperature (" +
                           Moose::stringify(_temperature_min) + ", " +
                           Moose::stringify(_temperature_max) + ").");
    else
    {
      temperature = max(T(_temperature_min), min(temperature, T(_temperature_max)));
      if (_OOBBehavior == DeclareInvalid)
        flagInvalidSolution("Temperature out of bounds");
      else if (_OOBBehavior == WarnInvalid)
        flagSolutionWarning("Temperature out of bounds");
    }
  }
}

Referenced by c_from_p_T(), c_from_p_T(), cp_from_p_T(), cp_from_p_T(), cv_from_p_T(), cv_from_p_T(), e_from_p_rho(), e_from_p_T(), e_from_p_T(), e_from_p_T(), h_from_p_T(), h_from_p_T(), h_from_p_T(), k_from_p_T(), k_from_p_T(), mu_from_p_T(), mu_from_p_T(), rho_from_p_T(), rho_from_p_T(), rho_from_p_T(), rho_from_p_T(), s_from_p_T(), s_from_p_T(), T_from_p_rho(), v_from_p_T(), v_from_p_T(), and v_from_p_T().

◆ checkInputVariablesVE()

template<typename T >

template void TabulatedFluidProperties::checkInputVariablesVE	(	T &	v,
		T &	e
	)		const

protected

Checks that the inputs are within the range of the tabulated data, and throws an error if they are not.

Parameters

v	specific volume (m3/kg)
e	specific internal energy (J/kg)

Definition at line 2268 of file TabulatedFluidProperties.C.

{
  using std::max, std::min;
 
  if (_OOBBehavior == Ignore)
    return;
  else if (e < _e_min || e > _e_max)
  {
    if (_OOBBehavior == Throw)
      throw MooseException("Specific internal energy " + Moose::stringify(e) +
                           " is outside the range of tabulated specific internal energies (" +
                           Moose::stringify(_e_min) + ", " + Moose::stringify(_e_max) + ").");
    else
    {
      e = max(_e_min, min(e, _e_max));
      if (_OOBBehavior == DeclareInvalid)
        flagInvalidSolution("Specific internal energy out of bounds");
      else if (_OOBBehavior == WarnInvalid)
        flagSolutionWarning("Specific internal energy out of bounds");
    }
  }
 
  if (v < _v_min || v > _v_max)
  {
    if (_OOBBehavior == Throw)
      throw MooseException("Specific volume " + Moose::stringify(v) +
                           " is outside the range of tabulated specific volumes (" +
                           Moose::stringify(_v_min) + ", " + Moose::stringify(_v_max) + ").");
    else
    {
      v = max(T(_v_min), min(v, T(_v_max)));
      if (_OOBBehavior == DeclareInvalid)
        flagInvalidSolution("Specific volume out of bounds");
      else if (_OOBBehavior == WarnInvalid)
        flagSolutionWarning("Specific volume out of bounds");
    }
  }
}

Referenced by c_from_v_e(), c_from_v_e(), cp_from_v_e(), cp_from_v_e(), cv_from_v_e(), cv_from_v_e(), g_from_v_e(), k_from_v_e(), k_from_v_e(), mu_from_v_e(), mu_from_v_e(), p_from_v_e(), p_from_v_e(), p_from_v_e(), s_from_v_e(), s_from_v_e(), T_from_v_e(), T_from_v_e(), and T_from_v_e().

◆ computePropertyIndicesInInterpolationVectors()

void TabulatedFluidProperties::computePropertyIndicesInInterpolationVectors ( )

protected

Retrieves the index for each property in the vector of interpolations.

Definition at line 2561 of file TabulatedFluidProperties.C.

{
  // At this point, all properties read or generated are able to be used by
  // TabulatedFluidProperties. Now set flags and indexes for each property in
  //_interpolated_properties to use in property calculations
  for (std::size_t i = 0; i < _interpolated_properties.size(); ++i)
  {
    if (_interpolated_properties[i] == "density")
    {
      _interpolate_density = true;
      _density_idx = i;
    }
    else if (_interpolated_properties[i] == "enthalpy")
    {
      _interpolate_enthalpy = true;
      _enthalpy_idx = i;
    }
    else if (_interpolated_properties[i] == "internal_energy")
    {
      _interpolate_internal_energy = true;
      _internal_energy_idx = i;
    }
    else if (_interpolated_properties[i] == "viscosity")
    {
      _interpolate_viscosity = true;
      _viscosity_idx = i;
    }
    else if (_interpolated_properties[i] == "k")
    {
      _interpolate_k = true;
      _k_idx = i;
    }
    else if (_interpolated_properties[i] == "c")
    {
      _interpolate_c = true;
      _c_idx = i;
    }
    else if (_interpolated_properties[i] == "cp")
    {
      _interpolate_cp = true;
      _cp_idx = i;
    }
    else if (_interpolated_properties[i] == "cv")
    {
      _interpolate_cv = true;
      _cv_idx = i;
    }
    else if (_interpolated_properties[i] == "entropy")
    {
      _interpolate_entropy = true;
      _entropy_idx = i;
    }
    else if (_interpolated_properties[i] == "pressure")
    {
      _interpolate_pressure = true;
      _p_idx = i;
    }
    else if (_interpolated_properties[i] == "temperature")
    {
      _interpolate_temperature = true;
      _T_idx = i;
    }
    else
      mooseError("Specified property '" + _interpolated_properties[i] +
                 "' is present in the tabulation but is not currently leveraged by the code in the "
                 "TabulatedFluidProperties. If it is spelled correctly, then please contact a "
                 "MOOSE or fluid properties module developer.");
  }
}

Referenced by initialSetup().

◆ constructInterpolation()

virtual void TabulatedFluidProperties::constructInterpolation ( )

pure virtual

Implemented in TabulatedBicubicFluidProperties.

Referenced by initialSetup().

◆ cp_from_p_T() [1/2]

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

overridevirtual

Definition at line 1057 of file TabulatedFluidProperties.C.

{
  if (_interpolate_cp && _create_direct_pT_interpolations)
  {
    checkInputVariables(pressure, temperature);
    return _property_ipol[_cp_idx]->sample(pressure, temperature);
  }
  else
  {
    if (_fp)
      return _fp->cp_from_p_T(pressure, temperature);
    else
      NeedTabulationOrFPError("cp_from_p_T", "c");
  }
}

Referenced by cp_from_v_e(), and cp_from_v_e().

◆ cp_from_p_T() [2/2]

void TabulatedFluidProperties::cp_from_p_T	(	Real	pressure,
		Real	temperature,
		Real &	cp,
		Real &	dcp_dp,
		Real &	dcp_dT
	)		const

overridevirtual

Definition at line 1074 of file TabulatedFluidProperties.C.

{
  if (_interpolate_cp && _create_direct_pT_interpolations)
  {
    checkInputVariables(pressure, temperature);
    _property_ipol[_cp_idx]->sampleValueAndDerivatives(pressure, temperature, cp, dcp_dp, dcp_dT);
  }
  else
  {
    if (_fp)
      _fp->cp_from_p_T(pressure, temperature, cp, dcp_dp, dcp_dT);
    else
      NeedTabulationOrFPError("cp_from_p_T with derivatives", "cp");
  }
}

◆ cp_from_v_e() [1/2]

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

overridevirtual

Definition at line 1528 of file TabulatedFluidProperties.C.

{
  if (_interpolate_cp && !_construct_pT_from_ve && !_create_direct_ve_interpolations)
    missingVEInterpolationError(__PRETTY_FUNCTION__);
  checkInputVariablesVE(v, e);
 
  if (_create_direct_ve_interpolations && _interpolate_cp)
    return _property_ve_ipol[_cp_idx]->sample(v, e);
  else if (_construct_pT_from_ve)
  {
    Real p = _p_from_v_e_ipol->sample(v, e);
    Real T = _T_from_v_e_ipol->sample(v, e);
    return cp_from_p_T(p, T);
  }
  else if (_fp)
    return _fp->cp_from_v_e(v, e);
  else
    NeedTabulationOrFPError("cp_from_v_e", "cp");
}

Referenced by writeTabulatedData().

◆ cp_from_v_e() [2/2]

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

overridevirtual

Definition at line 1549 of file TabulatedFluidProperties.C.

{
  if (_interpolate_cp && !_construct_pT_from_ve && !_create_direct_ve_interpolations)
    missingVEInterpolationError(__PRETTY_FUNCTION__);
  checkInputVariablesVE(v, e);
 
  if (_create_direct_ve_interpolations && _interpolate_cp)
    _property_ve_ipol[_cp_idx]->sampleValueAndDerivatives(v, e, cp, dcp_dv, dcp_de);
  else if (_construct_pT_from_ve)
  {
    Real p, dp_dv, dp_de;
    _p_from_v_e_ipol->sampleValueAndDerivatives(v, e, p, dp_dv, dp_de);
    Real T, dT_dv, dT_de;
    _T_from_v_e_ipol->sampleValueAndDerivatives(v, e, T, dT_dv, dT_de);
    Real dcp_dp, dcp_dT;
    cp_from_p_T(p, T, cp, dcp_dp, dcp_dT);
    dcp_dv = dcp_dp * dp_dv + dcp_dT * dT_dv;
    dcp_de = dcp_dp * dp_de + dcp_dT * dT_de;
  }
  else if (_fp)
    _fp->cp_from_v_e(v, e, cp, dcp_dv, dcp_de);
  else
    NeedTabulationOrFPError("cp_from_v_e with derivatives", "cp");
}

◆ createVEGridVectors()

void TabulatedFluidProperties::createVEGridVectors ( )

protected

Definition at line 2685 of file TabulatedFluidProperties.C.

{
  createVGridVector();
  if (!_e_bounds_specified)
  {
    // if csv exists, get max and min values from csv file
    if (_interpolate_internal_energy)
    {
      _e_min = *std::min_element(_properties[_internal_energy_idx].begin(),
                                 _properties[_internal_energy_idx].end());
      _e_max = *std::max_element(_properties[_internal_energy_idx].begin(),
                                 _properties[_internal_energy_idx].end());
    }
    else if (_fp)
    {
      // extreme values of internal energy for the grid bounds
      Real e1 = _fp->e_from_p_T(_pressure_min, _temperature_min);
      Real e2 = _fp->e_from_p_T(_pressure_max, _temperature_min);
      Real e3 = _fp->e_from_p_T(_pressure_min, _temperature_max);
      Real e4 = _fp->e_from_p_T(_pressure_max, _temperature_max);
      _e_min = std::min({e1, e2, e3, e4});
      _e_max = std::max({e1, e2, e3, e4});
    }
    else
      mooseWarning("Unable to compute grid bounds in internal energy. Please specify the e_min/max "
                   "parameters");
  }
 
  // Create e grid for interpolation
  _internal_energy.resize(_num_e);
  if (_log_space_e)
  {
    // incrementing the exponent linearly will yield a log-spaced grid after taking the value to
    // the power of 10
    if (_e_min < 0)
      mooseError("Logarithmic grid in specific energy can only be used with a positive specific "
                 "energy. Current minimum: " +
                 std::to_string(_e_min));
    Real de = (std::log10(_e_max) - std::log10(_e_min)) / ((Real)_num_e - 1);
    Real log_e_min = std::log10(_e_min);
    for (const auto j : make_range(_num_e))
      _internal_energy[j] = std::pow(10, log_e_min + j * de);
  }
  else
  {
    Real de = (_e_max - _e_min) / ((Real)_num_e - 1);
    for (const auto j : make_range(_num_e))
      _internal_energy[j] = _e_min + j * de;
  }
}

Referenced by TabulatedBicubicFluidProperties::constructInterpolation(), generateVETabulatedData(), and initialSetup().

◆ createVGridVector()

void TabulatedFluidProperties::createVGridVector ( )

protected

Create (or reset) the grid vectors for the specific volume and internal energy interpolations The order of priority for determining the range boundaries in v and e:

if user-specified, use _v_min/max and _e_min/max
if reading a (v,e) interpolation, the bounds of that range
if a _fp exist find the min/max v/e from T_min/max and p_min/max

Definition at line 2632 of file TabulatedFluidProperties.C.

{
  mooseAssert(_file_name_ve_in.empty(), "We should be reading the specific volume grid from file");
  if (!_v_bounds_specified)
  {
    // if csv exists, get max and min values from csv file
    if (_interpolate_density)
    {
      Real rho_max =
          *std::max_element(_properties[_density_idx].begin(), _properties[_density_idx].end());
      Real rho_min =
          *std::min_element(_properties[_density_idx].begin(), _properties[_density_idx].end());
      _v_max = 1 / rho_min;
      _v_min = 1 / rho_max;
    }
    else if (_fp)
    {
      // extreme values of specific volume for the grid bounds
      Real v1 = _fp->v_from_p_T(_pressure_min, _temperature_min);
      Real v2 = _fp->v_from_p_T(_pressure_max, _temperature_min);
      Real v3 = _fp->v_from_p_T(_pressure_min, _temperature_max);
      Real v4 = _fp->v_from_p_T(_pressure_max, _temperature_max);
      _v_min = std::min({v1, v2, v3, v4});
      _v_max = std::max({v1, v2, v3, v4});
    }
    else
      mooseWarning("Unable to compute grid bounds in specific volume. Please specify the v_min/max "
                   "parameters");
 
    // Prevent changing the bounds of the grid
    _v_bounds_specified = true;
  }
 
  // Create v grid for interpolation
  _specific_volume.resize(_num_v);
  if (_log_space_v)
  {
    // incrementing the exponent linearly will yield a log-spaced grid after taking the value to
    // the power of 10
    Real dv = (std::log10(_v_max) - std::log10(_v_min)) / ((Real)_num_v - 1);
    Real log_v_min = std::log10(_v_min);
    for (unsigned int j = 0; j < _num_v; ++j)
      _specific_volume[j] = std::pow(10, log_v_min + j * dv);
  }
  else
  {
    Real dv = (_v_max - _v_min) / ((Real)_num_v - 1);
    for (unsigned int j = 0; j < _num_v; ++j)
      _specific_volume[j] = _v_min + j * dv;
  }
}

Referenced by createVEGridVectors(), and createVHGridVectors().

◆ createVHGridVectors()

void TabulatedFluidProperties::createVHGridVectors ( )

protected

Create (or reset) the grid vectors for the specific volume and enthalpy interpolation The order of priority for determining the range boundaries in v and h:

if user-specified, use _v_min/max and _e_min/max
if a _fp exist find the min/max v/e from T_min/max and p_min/max
if reading a (p,T) tabulation, the bounds of the enthalpy grid
if reading a (v,e) tabulation, the bounds of the enthalpy grid

Definition at line 2737 of file TabulatedFluidProperties.C.

{
  if (_file_name_ve_in.empty())
    createVGridVector();
  if (_fp)
  {
    // extreme values of enthalpy for the grid bounds
    Real h1 = _fp->h_from_p_T(_pressure_min, _temperature_min);
    Real h2 = _fp->h_from_p_T(_pressure_max, _temperature_min);
    Real h3 = _fp->h_from_p_T(_pressure_min, _temperature_max);
    Real h4 = _fp->h_from_p_T(_pressure_max, _temperature_max);
    _h_min = std::min({h1, h2, h3, h4});
    _h_max = std::max({h1, h2, h3, h4});
  }
  // if csv exists, get max and min values from csv file
  else if (_properties.size())
  {
    _h_max = *max_element(_properties[_enthalpy_idx].begin(), _properties[_enthalpy_idx].end());
    _h_min = *min_element(_properties[_enthalpy_idx].begin(), _properties[_enthalpy_idx].end());
  }
  else if (_properties_ve.size())
  {
    _h_max = *max_element(_properties[_enthalpy_idx].begin(), _properties[_enthalpy_idx].end());
    _h_min = *min_element(_properties[_enthalpy_idx].begin(), _properties[_enthalpy_idx].end());
  }
  else
    mooseError("Need a source to compute the enthalpy grid bounds: either a FP object, or a (p,T) "
               "tabulation file or a (v,e) tabulation file");
 
  // Create h grid for interpolation
  // enthalpy & internal energy use same # grid points
  _enthalpy.resize(_num_e);
  if (_log_space_h)
  {
    // incrementing the exponent linearly will yield a log-spaced grid after taking the value to
    // the power of 10
    if (_h_min < 0)
      mooseError("Logarithmic grid in specific energy can only be used with a positive enthalpy. "
                 "Current minimum: " +
                 std::to_string(_h_min));
    Real dh = (std::log10(_h_max) - std::log10(_h_min)) / ((Real)_num_e - 1);
    Real log_h_min = std::log10(_h_min);
    for (const auto j : make_range(_num_e))
      _enthalpy[j] = std::pow(10, log_h_min + j * dh);
  }
  else
  {
    Real dh = (_h_max - _h_min) / ((Real)_num_e - 1);
    for (const auto j : make_range(_num_e))
      _enthalpy[j] = _h_min + j * dh;
  }
}

Referenced by TabulatedBicubicFluidProperties::constructInterpolation().

◆ criticalDensity()

Real TabulatedFluidProperties::criticalDensity ( ) const

overridevirtual

Critical density.

Returns: critical density (kg/m^3)

Reimplemented from SinglePhaseFluidProperties.

Definition at line 1366 of file TabulatedFluidProperties.C.

{
  if (_fp)
    return _fp->criticalDensity();
  else
    TabulationNotImplementedError("criticalDensity");
}

◆ criticalInternalEnergy()

Real SinglePhaseFluidProperties::criticalInternalEnergy ( ) const

virtualinherited

Critical specific internal energy.

Returns: specific internal energy (J/kg)

Reimplemented in CaloricallyImperfectGas, IdealGasFluidProperties, and StiffenedGasFluidProperties.

Definition at line 320 of file SinglePhaseFluidProperties.C.

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

◆ criticalPressure()

Real TabulatedFluidProperties::criticalPressure ( ) const

overridevirtual

Critical pressure.

Returns: critical pressure (Pa)

Reimplemented from SinglePhaseFluidProperties.

Definition at line 1346 of file TabulatedFluidProperties.C.

{
 
  if (_fp)
    return _fp->criticalPressure();
  else
    TabulationNotImplementedError("criticalPressure");
}

◆ criticalTemperature()

Real TabulatedFluidProperties::criticalTemperature ( ) const

overridevirtual

Critical temperature.

Returns: critical temperature (K)

Reimplemented from SinglePhaseFluidProperties.

Definition at line 1356 of file TabulatedFluidProperties.C.

{
 
  if (_fp)
    return _fp->criticalTemperature();
  else
    TabulationNotImplementedError("criticalTemperature");
}

◆ cv_from_p_T() [1/2]

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

overridevirtual

Definition at line 1092 of file TabulatedFluidProperties.C.

{
  if (_interpolate_cv && _create_direct_pT_interpolations)
  {
    checkInputVariables(pressure, temperature);
    return _property_ipol[_cv_idx]->sample(pressure, temperature);
  }
  else
  {
    if (_fp)
      return _fp->cv_from_p_T(pressure, temperature);
    else
      NeedTabulationOrFPError("cv_from_p_T", "cv");
  }
}

Referenced by cv_from_v_e(), and cv_from_v_e().

◆ cv_from_p_T() [2/2]

void TabulatedFluidProperties::cv_from_p_T	(	Real	pressure,
		Real	temperature,
		Real &	cv,
		Real &	dcv_dp,
		Real &	dcv_dT
	)		const

overridevirtual

Definition at line 1109 of file TabulatedFluidProperties.C.

{
  if (_interpolate_cv)
  {
    checkInputVariables(pressure, temperature);
    _property_ipol[_cv_idx]->sampleValueAndDerivatives(pressure, temperature, cv, dcv_dp, dcv_dT);
  }
  else
  {
    if (_fp)
      _fp->cv_from_p_T(pressure, temperature, cv, dcv_dp, dcv_dT);
    else
      NeedTabulationOrFPError("cv_from_p_T with derivatives", "cv");
  }
}

◆ cv_from_v_e() [1/2]

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

overridevirtual

Definition at line 1575 of file TabulatedFluidProperties.C.

{
  if (_interpolate_cv && !_construct_pT_from_ve && !_create_direct_ve_interpolations)
    missingVEInterpolationError(__PRETTY_FUNCTION__);
  checkInputVariablesVE(v, e);
 
  if (_create_direct_ve_interpolations && _interpolate_cv)
    return _property_ve_ipol[_cv_idx]->sample(v, e);
  else if (_construct_pT_from_ve)
  {
    Real p = _p_from_v_e_ipol->sample(v, e);
    Real T = _T_from_v_e_ipol->sample(v, e);
    return cv_from_p_T(p, T);
  }
  else if (_fp)
    return _fp->cv_from_v_e(v, e);
  else
    NeedTabulationOrFPError("cv_from_v_e", "cv");
}

Referenced by writeTabulatedData().

◆ cv_from_v_e() [2/2]

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

overridevirtual

Definition at line 1596 of file TabulatedFluidProperties.C.

{
  if (_interpolate_cv && !_construct_pT_from_ve && !_create_direct_ve_interpolations)
    missingVEInterpolationError(__PRETTY_FUNCTION__);
  checkInputVariablesVE(v, e);
 
  if (_create_direct_ve_interpolations && _interpolate_cv)
    _property_ve_ipol[_cv_idx]->sampleValueAndDerivatives(v, e, cv, dcv_dv, dcv_de);
  else if (_construct_pT_from_ve)
  {
    Real p, dp_dv, dp_de;
    _p_from_v_e_ipol->sampleValueAndDerivatives(v, e, p, dp_dv, dp_de);
    Real T, dT_dv, dT_de;
    _T_from_v_e_ipol->sampleValueAndDerivatives(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;
  }
  else if (_fp)
    _fp->cv_from_v_e(v, e, cv, dcv_dv, dcv_de);
  else
    NeedTabulationOrFPError("cv_from_v_e with derivatives", "cv");
}

◆ e_from_p_rho() [1/3]

ADReal TabulatedFluidProperties::e_from_p_rho	(	const ADReal &	pressure,
		const ADReal &	rho
	)		const

overridevirtual

Definition at line 716 of file TabulatedFluidProperties.C.

{
  ADReal e;
  // Use v,e data, we already have v from rho
  if (_create_direct_ve_interpolations)
  {
    auto lambda = [&](ADReal v, ADReal current_e, ADReal & new_p, ADReal & dp_dv, ADReal & dp_de)
    { p_from_v_e(v, current_e, new_p, dp_dv, dp_de); };
    const auto pair = FluidPropertiesUtils::NewtonSolve(1. / rho,
                                                        pressure,
                                                        /*initial guess*/ (_e_min + _e_max) / 2,
                                                        _tolerance,
                                                        lambda,
                                                        name() + "::e_from_p_rho",
                                                        _max_newton_its,
                                                        _verbose_newton);
    e = pair.first;
  }
  // May use rho_from_p_T with derivatives in a Newton solve
  else
  {
    const auto T = T_from_p_rho(pressure, rho);
    e = e_from_p_T(pressure, T);
  }
  return e;
}

◆ e_from_p_rho() [2/3]

Real TabulatedFluidProperties::e_from_p_rho	(	Real	pressure,
		Real	rho
	)		const

overridevirtual

Definition at line 744 of file TabulatedFluidProperties.C.

{
  Real e;
  // Use v,e data, we already have v from rho
  if (_create_direct_ve_interpolations)
  {
    Real T_dummy = _T_initial_guess;
    checkInputVariables(pressure, T_dummy);
    auto lambda = [&](Real v, Real current_e, Real & new_p, Real & dp_dv, Real & dp_de)
    { p_from_v_e(v, current_e, new_p, dp_dv, dp_de); };
    const auto pair = FluidPropertiesUtils::NewtonSolve(1. / rho,
                                                        pressure,
                                                        /*initial guess*/ (_e_min + _e_max) / 2,
                                                        _tolerance,
                                                        lambda,
                                                        name() + "::e_from_p_rho",
                                                        _max_newton_its,
                                                        _verbose_newton);
    e = pair.first;
  }
  // May use rho_from_p_T with derivatives in a Newton solve
  else
  {
    Real T = T_from_p_rho(pressure, rho);
    e = e_from_p_T(pressure, T);
  }
  return e;
}

Referenced by T_from_p_rho(), and T_from_p_rho().

◆ e_from_p_rho() [3/3]

void TabulatedFluidProperties::e_from_p_rho	(	Real	pressure,
		Real	rho,
		Real &	e,
		Real &	de_dp,
		Real &	de_drho
	)		const

overridevirtual

Definition at line 774 of file TabulatedFluidProperties.C.

{
  // get derivatives of T wrt to pressure and density
  Real T, dT_dp, dT_drho;
  T_from_p_rho(pressure, rho, T, dT_dp, dT_drho);
 
  // Get e, then derivatives of e wrt pressure and temperature
  Real de_dp_at_const_T, de_dT;
  e_from_p_T(pressure, T, e, de_dp_at_const_T, de_dT);
 
  // Get the derivatives of density wrt pressure and temperature
  Real rho_pT, drho_dp, drho_dT;
  rho_from_p_T(pressure, T, rho_pT, drho_dp, drho_dT);
 
  // derivatives of e wrt pressure and rho (what we want from e_from_p_rho)
  de_drho = de_dT * dT_drho;
  de_dp = de_dp_at_const_T - (de_drho * drho_dp);
}

◆ e_from_p_T() [1/3]

ADReal TabulatedFluidProperties::e_from_p_T	(	const ADReal &	pressure,
		const ADReal &	temperature
	)		const

overridevirtual

Definition at line 647 of file TabulatedFluidProperties.C.

{
  if (_interpolate_internal_energy)
  {
    ADReal pressure_nc = pressure, temperature_nc = temperature;
    checkInputVariables(pressure_nc, temperature_nc);
    if (_create_direct_pT_interpolations)
      return _property_ipol[_internal_energy_idx]->sample(pressure_nc, temperature_nc);
    else
      NeedTabulationError("internal_energy");
  }
  else if (_create_direct_ve_interpolations)
  {
    ADReal pressure_nc = pressure, temperature_nc = temperature;
    checkInputVariables(pressure_nc, temperature_nc);
    const ADReal rho = rho_from_p_T(pressure_nc, temperature_nc);
    auto lambda = [&](ADReal v, ADReal current_e, ADReal & new_T, ADReal & dT_dv, ADReal & dT_de)
    { T_from_v_e(v, current_e, new_T, dT_dv, dT_de); };
    const auto pair = FluidPropertiesUtils::NewtonSolve(1. / rho,
                                                        temperature_nc,
                                                        /*initial guess*/ (_e_min + _e_max) / 2,
                                                        _tolerance,
                                                        lambda,
                                                        name() + "::e_from_p_T",
                                                        _max_newton_its,
                                                        _verbose_newton);
    return pair.first;
  }
  else
  {
    if (_fp)
      return _fp->e_from_p_T(pressure, temperature);
    else
      NeedTabulationOrFPError("AD e_from_p_T", "internal_energy");
  }
}

◆ e_from_p_T() [2/3]

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

overridevirtual

Definition at line 611 of file TabulatedFluidProperties.C.

{
  if (_interpolate_internal_energy)
  {
    checkInputVariables(pressure, temperature);
    if (_create_direct_pT_interpolations)
      return _property_ipol[_internal_energy_idx]->sample(pressure, temperature);
    else
      NeedTabulationError("internal_energy");
  }
  else if (_create_direct_ve_interpolations)
  {
    checkInputVariables(pressure, temperature);
    const Real rho = rho_from_p_T(pressure, temperature);
    auto lambda = [&](Real v, Real current_e, Real & new_T, Real & dT_dv, Real & dT_de)
    { T_from_v_e(v, current_e, new_T, dT_dv, dT_de); };
    const auto pair = FluidPropertiesUtils::NewtonSolve(1. / rho,
                                                        temperature,
                                                        /*initial guess*/ (_e_min + _e_max) / 2,
                                                        _tolerance,
                                                        lambda,
                                                        name() + "::e_from_p_T",
                                                        _max_newton_its,
                                                        _verbose_newton);
    return pair.first;
  }
  else
  {
    if (_fp)
      return _fp->e_from_p_T(pressure, temperature);
    else
      NeedTabulationOrFPError("e_from_p_T", "internal_energy");
  }
}

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

◆ e_from_p_T() [3/3]

void TabulatedFluidProperties::e_from_p_T	(	Real	pressure,
		Real	temperature,
		Real &	e,
		Real &	de_dp,
		Real &	de_dT
	)		const

overridevirtual

Definition at line 685 of file TabulatedFluidProperties.C.

{
  if (_interpolate_internal_energy)
  {
    checkInputVariables(pressure, temperature);
    if (_create_direct_pT_interpolations)
      _property_ipol[_internal_energy_idx]->sampleValueAndDerivatives(
          pressure, temperature, e, de_dp, de_dT);
    else
      NeedTabulationError("internal_energy");
  }
  else if (_create_direct_ve_interpolations)
  {
    checkInputVariables(pressure, temperature);
    // use finite differencing stencil
    e = e_from_p_T(pressure, temperature);
    Real eps = 1e-8;
    de_dp = (e_from_p_T(pressure * (1 + eps), temperature) - e) / (eps * pressure);
    de_dT = (e_from_p_T(pressure, temperature * (1 + eps)) - e) / (eps * temperature);
  }
  else
  {
    if (_fp)
      _fp->e_from_p_T(pressure, temperature, e, de_dp, de_dT);
    else
      NeedTabulationOrFPError("e_from_p_T with derivatives", "internal_energy");
  }
}

◆ e_from_v_h() [1/2]

Real TabulatedFluidProperties::e_from_v_h	(	Real	v,
		Real	h
	)		const

overridevirtual

Definition at line 1209 of file TabulatedFluidProperties.C.

{
  if (_construct_pT_from_vh)
  {
    const Real p = _p_from_v_h_ipol->sample(v, h);
    const Real T = _T_from_v_h_ipol->sample(v, h);
    return e_from_p_T(p, T);
  }
  else if (_create_direct_ve_interpolations)
  {
    // Lambda computes h from v and the current_e
    auto lambda = [&](Real v, Real current_e, Real & new_h, Real & dh_dv, Real & dh_de)
    { h_from_v_e(v, current_e, new_h, dh_dv, dh_de); };
    Real e = FluidPropertiesUtils::NewtonSolve(v,
                                               h,
                                               /*e initial guess*/ h - _p_initial_guess * v,
                                               _tolerance,
                                               lambda,
                                               name() + "::e_from_v_h",
                                               _max_newton_its,
                                               _verbose_newton)
                 .first;
    return e;
  }
  else if (_fp)
    return _fp->e_from_v_h(v, h);
  else
    NeedTabulationOrFPError("e_from_v_h", "internal_energy");
}

Referenced by e_from_v_h().

◆ e_from_v_h() [2/2]

void TabulatedFluidProperties::e_from_v_h	(	Real	v,
		Real	h,
		Real &	e,
		Real &	de_dv,
		Real &	de_dh
	)		const

overridevirtual

Definition at line 1240 of file TabulatedFluidProperties.C.

{
  if (_construct_pT_from_vh)
  {
    Real p = 0, dp_dv = 0, dp_dh = 0;
    _p_from_v_h_ipol->sampleValueAndDerivatives(v, h, p, dp_dv, dp_dh);
    Real T = 0, dT_dv = 0, dT_dh = 0;
    _T_from_v_h_ipol->sampleValueAndDerivatives(v, h, T, dT_dv, dT_dh);
    Real de_dp, de_dT;
    e_from_p_T(p, T, e, de_dp, de_dT);
    de_dv = de_dp * dp_dv + de_dT * dT_dv;
    de_dh = de_dp * dp_dh + de_dT * dT_dh;
  }
  else if (_create_direct_ve_interpolations)
  {
    // Lambda computes h from v and the current_e
    auto lambda = [&](Real v, Real current_e, Real & new_h, Real & dh_dv, Real & dh_de)
    { h_from_v_e(v, current_e, new_h, dh_dv, dh_de); };
    const auto e_data =
        FluidPropertiesUtils::NewtonSolve(v,
                                          h,
                                          /*e initial guess*/ h - _p_initial_guess * v,
                                          _tolerance,
                                          lambda,
                                          name() + "::e_from_v_h",
                                          _max_newton_its,
                                          _verbose_newton);
    e = e_data.first;
    // Finite difference approximation
    const auto e2 = e_from_v_h(v * (1 + TOLERANCE), h);
    de_dv = (e2 - e) / (TOLERANCE * v);
    de_dh = 1. / e_data.second;
  }
  else if (_fp)
    _fp->e_from_v_h(v, h, e, de_dv, de_dh);
  else
    NeedTabulationOrFPError("e_from_v_h", "internal_energy");
}

◆ 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 CaloricallyImperfectGas, IdealGasFluidProperties, 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 TabulatedFluidProperties::fluidName ( ) const

overridevirtual

Fluid name.

Returns: string representing fluid name

Reimplemented from SinglePhaseFluidProperties.

Definition at line 379 of file TabulatedFluidProperties.C.

{
  if (_fp)
    return _fp->fluidName();
  else
    return "TabulationFromFile";
}

◆ g_from_v_e()

Real TabulatedFluidProperties::g_from_v_e	(	Real	v,
		Real	e
	)		const

overridevirtual

Definition at line 1762 of file TabulatedFluidProperties.C.

{
  if (!_construct_pT_from_ve &&
      (!_create_direct_ve_interpolations || _entropy_idx == libMesh::invalid_uint ||
       _enthalpy_idx == libMesh::invalid_uint || _T_idx == libMesh::invalid_uint))
    missingVEInterpolationError(__PRETTY_FUNCTION__);
  checkInputVariablesVE(v, e);
 
  Real h, T = 0, s;
  if (_create_direct_ve_interpolations)
  {
    s = _property_ve_ipol[_entropy_idx]->sample(v, e);
    h = _property_ve_ipol[_enthalpy_idx]->sample(v, e);
    T = _property_ve_ipol[_T_idx]->sample(v, e);
  }
  else if (_fp || _create_direct_pT_interpolations)
  {
    Real p0 = _p_initial_guess;
    Real T0 = _T_initial_guess;
    Real p = 0;
    bool conversion_succeeded;
    p_T_from_v_e(v, e, p0, T0, p, T, conversion_succeeded);
    s = s_from_p_T(p, T);
    h = h_from_p_T(p, T);
  }
  else
    mooseError(__PRETTY_FUNCTION__,
               "\nNo tabulation or fluid property 'input_fp' object to compute value");
  return h - T * s;
}

◆ generateTabulatedData()

void TabulatedFluidProperties::generateTabulatedData ( )

protectedvirtual

Generates a table of fluid properties by looping over pressure and temperature and calculating properties using the FluidProperties UserObject _fp.

Definition at line 2051 of file TabulatedFluidProperties.C.

{
  mooseAssert(_fp, "We should not try to generate (p,T) tabulated data without a _fp user object");
  _pressure.resize(_num_p);
  _temperature.resize(_num_T);
 
  // Generate data for all properties entered in input file
  _properties.resize(_interpolated_properties_enum.size());
  _interpolated_properties.resize(_interpolated_properties_enum.size());
 
  for (std::size_t i = 0; i < _interpolated_properties_enum.size(); ++i)
    _interpolated_properties[i] = _interpolated_properties_enum[i];
 
  for (const auto i : index_range(_properties))
    _properties[i].resize(_num_p * _num_T);
 
  // Temperature is divided equally into _num_T segments
  Real delta_T = (_temperature_max - _temperature_min) / static_cast<Real>(_num_T - 1);
 
  for (unsigned int j = 0; j < _num_T; ++j)
    _temperature[j] = _temperature_min + j * delta_T;
 
  // Divide the pressure into _num_p equal segments
  Real delta_p = (_pressure_max - _pressure_min) / static_cast<Real>(_num_p - 1);
 
  for (unsigned int i = 0; i < _num_p; ++i)
    _pressure[i] = _pressure_min + i * delta_p;
 
  // Generate the tabulated data at the pressure and temperature points
  for (const auto i : index_range(_properties))
  {
    if (_interpolated_properties[i] == "density")
      for (unsigned int p = 0; p < _num_p; ++p)
        for (unsigned int t = 0; t < _num_T; ++t)
          _properties[i][p * _num_T + t] = _fp->rho_from_p_T(_pressure[p], _temperature[t]);
 
    if (_interpolated_properties[i] == "enthalpy")
      for (unsigned int p = 0; p < _num_p; ++p)
        for (unsigned int t = 0; t < _num_T; ++t)
          _properties[i][p * _num_T + t] = _fp->h_from_p_T(_pressure[p], _temperature[t]);
 
    if (_interpolated_properties[i] == "internal_energy")
      for (unsigned int p = 0; p < _num_p; ++p)
        for (unsigned int t = 0; t < _num_T; ++t)
          _properties[i][p * _num_T + t] = _fp->e_from_p_T(_pressure[p], _temperature[t]);
 
    if (_interpolated_properties[i] == "viscosity")
      for (unsigned int p = 0; p < _num_p; ++p)
        for (unsigned int t = 0; t < _num_T; ++t)
          _properties[i][p * _num_T + t] = _fp->mu_from_p_T(_pressure[p], _temperature[t]);
 
    if (_interpolated_properties[i] == "k")
      for (unsigned int p = 0; p < _num_p; ++p)
        for (unsigned int t = 0; t < _num_T; ++t)
          _properties[i][p * _num_T + t] = _fp->k_from_p_T(_pressure[p], _temperature[t]);
 
    if (_interpolated_properties[i] == "c")
      for (unsigned int p = 0; p < _num_p; ++p)
        for (unsigned int t = 0; t < _num_T; ++t)
          _properties[i][p * _num_T + t] = _fp->c_from_p_T(_pressure[p], _temperature[t]);
 
    if (_interpolated_properties[i] == "cv")
      for (unsigned int p = 0; p < _num_p; ++p)
        for (unsigned int t = 0; t < _num_T; ++t)
          _properties[i][p * _num_T + t] = _fp->cv_from_p_T(_pressure[p], _temperature[t]);
 
    if (_interpolated_properties[i] == "cp")
      for (unsigned int p = 0; p < _num_p; ++p)
        for (unsigned int t = 0; t < _num_T; ++t)
          _properties[i][p * _num_T + t] = _fp->cp_from_p_T(_pressure[p], _temperature[t]);
 
    if (_interpolated_properties[i] == "entropy")
      for (unsigned int p = 0; p < _num_p; ++p)
        for (unsigned int t = 0; t < _num_T; ++t)
          _properties[i][p * _num_T + t] = _fp->s_from_p_T(_pressure[p], _temperature[t]);
  }
}

Referenced by initialSetup().

◆ generateVETabulatedData()

void TabulatedFluidProperties::generateVETabulatedData ( )

protectedvirtual

Generates a table of fluid properties by looping over specific volume and internal energy and calculating properties using the FluidProperties UserObject _fp.

Definition at line 2130 of file TabulatedFluidProperties.C.

{
  mooseAssert(_fp, "We should not try to generate (v,e) tabulated data without a _fp user object");
  _specific_volume.resize(_num_v);
  _internal_energy.resize(_num_e);
 
  // Generate data for all properties entered in input file
  _properties_ve.resize(_interpolated_properties_enum.size());
  _interpolated_properties.resize(_interpolated_properties_enum.size());
 
  // This is filled from the user input, so it does not matter than this operation is performed
  // for both the (p,T) and (v,e) tabulated data generation
  for (std::size_t i = 0; i < _interpolated_properties_enum.size(); ++i)
    _interpolated_properties[i] = _interpolated_properties_enum[i];
 
  for (const auto i : index_range(_properties_ve))
    _properties_ve[i].resize(_num_v * _num_e);
 
  // Grids in (v,e) are not read, so we either use user input or rely on (p,T) data
  createVEGridVectors();
 
  // Generate the tabulated data at the pressure and temperature points
  for (const auto i : index_range(_properties_ve))
  {
    if (_interpolated_properties[i] == "density")
      for (unsigned int v = 0; v < _num_v; ++v)
        for (unsigned int e = 0; e < _num_e; ++e)
          _properties_ve[i][v * _num_e + e] = 1. / _specific_volume[v];
 
    if (_interpolated_properties[i] == "enthalpy")
      for (unsigned int v = 0; v < _num_v; ++v)
        for (unsigned int e = 0; e < _num_e; ++e)
          _properties_ve[i][v * _num_e + e] =
              _fp->h_from_v_e(_specific_volume[v], _internal_energy[e]);
 
    if (_interpolated_properties[i] == "internal_energy")
      for (unsigned int v = 0; v < _num_v; ++v)
        for (unsigned int e = 0; e < _num_e; ++e)
          _properties_ve[i][v * _num_e + e] = _internal_energy[e];
 
    if (_interpolated_properties[i] == "viscosity")
      for (unsigned int v = 0; v < _num_v; ++v)
        for (unsigned int e = 0; e < _num_e; ++e)
          _properties_ve[i][v * _num_e + e] =
              _fp->mu_from_v_e(_specific_volume[v], _internal_energy[e]);
 
    if (_interpolated_properties[i] == "k")
      for (unsigned int v = 0; v < _num_v; ++v)
        for (unsigned int e = 0; e < _num_e; ++e)
          _properties_ve[i][v * _num_e + e] =
              _fp->k_from_v_e(_specific_volume[v], _internal_energy[e]);
 
    if (_interpolated_properties[i] == "c")
      for (unsigned int v = 0; v < _num_v; ++v)
        for (unsigned int e = 0; e < _num_e; ++e)
          _properties_ve[i][v * _num_e + e] =
              _fp->c_from_v_e(_specific_volume[v], _internal_energy[e]);
 
    if (_interpolated_properties[i] == "cv")
      for (unsigned int v = 0; v < _num_v; ++v)
        for (unsigned int e = 0; e < _num_e; ++e)
          _properties_ve[i][v * _num_e + e] =
              _fp->cv_from_v_e(_specific_volume[v], _internal_energy[e]);
 
    if (_interpolated_properties[i] == "cp")
      for (unsigned int v = 0; v < _num_v; ++v)
        for (unsigned int e = 0; e < _num_e; ++e)
          _properties_ve[i][v * _num_e + e] =
              _fp->cp_from_v_e(_specific_volume[v], _internal_energy[e]);
 
    if (_interpolated_properties[i] == "entropy")
      for (unsigned int v = 0; v < _num_v; ++v)
        for (unsigned int e = 0; e < _num_e; ++e)
          _properties_ve[i][v * _num_e + e] =
              _fp->s_from_v_e(_specific_volume[v], _internal_energy[e]);
 
    if (_interpolated_properties[i] == "pressure")
      for (unsigned int v = 0; v < _num_v; ++v)
        for (unsigned int e = 0; e < _num_e; ++e)
          _properties_ve[i][v * _num_e + e] =
              _fp->p_from_v_e(_specific_volume[v], _internal_energy[e]);
 
    if (_interpolated_properties[i] == "temperature")
      for (unsigned int v = 0; v < _num_v; ++v)
        for (unsigned int e = 0; e < _num_e; ++e)
          _properties_ve[i][v * _num_e + e] =
              _fp->T_from_v_e(_specific_volume[v], _internal_energy[e]);
  }
}

Referenced by initialSetup().

◆ h_from_p_T() [1/3]

ADReal TabulatedFluidProperties::h_from_p_T	(	const ADReal &	pressure,
		const ADReal &	temperature
	)		const

overridevirtual

Definition at line 930 of file TabulatedFluidProperties.C.

{
  if (_interpolate_enthalpy)
  {
    ADReal pressure_nc = pressure, temperature_nc = temperature;
    checkInputVariables(pressure_nc, temperature_nc);
    if (_create_direct_pT_interpolations)
      return _property_ipol[_enthalpy_idx]->sample(pressure_nc, temperature_nc);
    else if (_create_direct_ve_interpolations)
    {
      ADReal v, e;
      SinglePhaseFluidProperties::v_e_from_p_T(pressure_nc, temperature_nc, v, e);
      return _property_ve_ipol[_enthalpy_idx]->sample(v, e);
    }
    else
      NeedTabulationError("enthalpy");
  }
  else if (_fp) // Assuming _fp can handle ADReal types
    return _fp->h_from_p_T(pressure, temperature);
  else
    NeedTabulationOrFPError("AD h_from_p_T", "enthalpy");
}

◆ h_from_p_T() [2/3]

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

overridevirtual

Definition at line 904 of file TabulatedFluidProperties.C.

{
  if (_interpolate_enthalpy)
  {
    checkInputVariables(pressure, temperature);
    if (_create_direct_pT_interpolations)
      return _property_ipol[_enthalpy_idx]->sample(pressure, temperature);
    else if (_create_direct_ve_interpolations)
    {
      Real v, e;
      SinglePhaseFluidProperties::v_e_from_p_T(pressure, temperature, v, e);
      return _property_ve_ipol[_enthalpy_idx]->sample(v, e);
    }
    else
      NeedTabulationError("enthalpy");
  }
  else
  {
    if (_fp)
      return _fp->h_from_p_T(pressure, temperature);
    else
      NeedTabulationOrFPError("h_from_p_T", "enthalpy");
  }
}

Referenced by g_from_v_e(), T_from_p_h(), and T_from_p_h().

◆ h_from_p_T() [3/3]

void TabulatedFluidProperties::h_from_p_T	(	Real	pressure,
		Real	temperature,
		Real &	h,
		Real &	dh_dp,
		Real &	dh_dT
	)		const

overridevirtual

Definition at line 954 of file TabulatedFluidProperties.C.

{
  if (_interpolate_enthalpy)
  {
    checkInputVariables(pressure, temperature);
    if (_create_direct_pT_interpolations)
      _property_ipol[_enthalpy_idx]->sampleValueAndDerivatives(
          pressure, temperature, h, dh_dp, dh_dT);
    else if (_create_direct_ve_interpolations)
    {
      Real v, e, dv_dp, dv_dT, de_dp, de_dT;
      SinglePhaseFluidProperties::v_e_from_p_T(
          pressure, temperature, v, dv_dp, dv_dT, e, de_dp, de_dT);
      Real dh_dv, dh_de;
      _property_ve_ipol[_enthalpy_idx]->sampleValueAndDerivatives(v, e, h, dh_dv, dh_de);
      dh_dp = dh_dv * dv_dp + dh_de * de_dp;
      dh_dT = dh_dv * dv_dT + dh_de * de_dT;
    }
    else
      NeedTabulationError("enthalpy");
  }
  else
  {
    if (_fp)
      _fp->h_from_p_T(pressure, temperature, h, dh_dp, dh_dT);
    else
      NeedTabulationOrFPError("h_from_p_T with derivatives", "enthalpy");
  }
}

◆ henryCoefficients()

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

overridevirtual

The following routines are simply forwarded to the 'fp' companion FluidProperties as they are not included in the tabulations presently.

Reimplemented from SinglePhaseFluidProperties.

Definition at line 1280 of file TabulatedFluidProperties.C.

{
  if (_fp)
    return _fp->henryCoefficients();
  else
    TabulationNotImplementedError("henryCoefficients");
}

◆ initialize()

virtual void FluidProperties::initialize ( )

inlinefinalvirtualinherited

Implements ThreadedGeneralUserObject.

Definition at line 34 of file FluidProperties.h.

34{}

◆ initialSetup()

void TabulatedFluidProperties::initialSetup ( )

overridevirtual

Reimplemented from ThreadedGeneralUserObject.

Definition at line 319 of file TabulatedFluidProperties.C.

{
  if (_initial_setup_done)
    return;
  _initial_setup_done = true;
 
  if (_create_direct_pT_interpolations)
  {
    // If the user specified a (p, T) tabulation to read, use that
    if (!_file_name_in.empty())
      readFileTabulationData(true);
    else
    {
      if (!_fp)
        paramError("create_pT_interpolations",
                   "No FluidProperties (specified with 'input_fp' parameter) exists. Either "
                   "specify a 'input_fp' or "
                   "specify a (p, T) tabulation file with the 'fluid_property_file' parameter");
      _console << name() + ": Generating (p, T) tabulated data\n";
      _console << std::flush;
 
      generateTabulatedData();
    }
  }
 
  if (_create_direct_ve_interpolations)
  {
    // If the user specified a (v, e) tabulation to read, use that
    if (!_file_name_ve_in.empty())
      readFileTabulationData(false);
    else
    {
      if (!_fp)
        paramError("create_ve_interpolations",
                   "No FluidProperties (specified with 'input_fp' parameter) exists. Either "
                   "specify a 'input_fp' or "
                   "specify a (v, e) tabulation file with the 'fluid_property_ve_file' parameter");
      _console << name() + ": Generating (v, e) tabulated data\n";
      _console << std::flush;
 
      generateVETabulatedData();
    }
  }
 
  computePropertyIndicesInInterpolationVectors();
  constructInterpolation();
 
  // Could be needed to get bounds computed from (p, T) bounds
  if (_fp && !_create_direct_ve_interpolations)
    createVEGridVectors();
 
  // Write tabulated data to file
  if (_save_file)
  {
    _console << name() + ": Writing tabulated data to " << _file_name_out << "\n";
    writeTabulatedData(_file_name_out);
  }
}

◆ k_from_p_T() [1/2]

Real TabulatedFluidProperties::k_from_p_T	(	Real	pressure,
		Real	temperature
	)		const

overridevirtual

Definition at line 1127 of file TabulatedFluidProperties.C.

{
  if (_interpolate_k && _create_direct_pT_interpolations)
  {
    checkInputVariables(pressure, temperature);
    return _property_ipol[_k_idx]->sample(pressure, temperature);
  }
  else
  {
    if (_fp)
      return _fp->k_from_p_T(pressure, temperature);
    else
      NeedTabulationOrFPError("k_from_p_T", "k");
  }
}

Referenced by k_from_v_e(), and k_from_v_e().

◆ k_from_p_T() [2/2]

void TabulatedFluidProperties::k_from_p_T	(	Real	pressure,
		Real	temperature,
		Real &	k,
		Real &	dk_dp,
		Real &	dk_dT
	)		const

overridevirtual

Definition at line 1144 of file TabulatedFluidProperties.C.

{
  if (_interpolate_k && _create_direct_pT_interpolations)
  {
    checkInputVariables(pressure, temperature);
    return _property_ipol[_k_idx]->sampleValueAndDerivatives(
        pressure, temperature, k, dk_dp, dk_dT);
  }
  else
  {
    if (_fp)
      return _fp->k_from_p_T(pressure, temperature, k, dk_dp, dk_dT);
    else
      NeedTabulationOrFPError("k_from_p_T with derivatives", "k");
  }
}

◆ k_from_v_e() [1/2]

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

overridevirtual

Definition at line 1669 of file TabulatedFluidProperties.C.

{
  if (_interpolate_k && !_construct_pT_from_ve && !_create_direct_ve_interpolations)
    missingVEInterpolationError(__PRETTY_FUNCTION__);
  checkInputVariablesVE(v, e);
 
  if (_create_direct_ve_interpolations && _interpolate_k)
    return _property_ve_ipol[_k_idx]->sample(v, e);
  else if (_construct_pT_from_ve)
  {
    Real T = _T_from_v_e_ipol->sample(v, e);
    Real p = _p_from_v_e_ipol->sample(v, e);
    return k_from_p_T(p, T);
  }
  else if (_fp)
    return _fp->k_from_v_e(v, e);
  else
    NeedTabulationOrFPError("k_from_v_e", "k");
}

Referenced by writeTabulatedData().

◆ k_from_v_e() [2/2]

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

overridevirtual

Definition at line 1690 of file TabulatedFluidProperties.C.

{
  if (_interpolate_k && !_construct_pT_from_ve && !_create_direct_ve_interpolations)
    missingVEInterpolationError(__PRETTY_FUNCTION__);
  checkInputVariablesVE(v, e);
 
  if (_create_direct_ve_interpolations && _interpolate_k)
    _property_ve_ipol[_k_idx]->sampleValueAndDerivatives(v, e, k, dk_dv, dk_de);
  else if (_construct_pT_from_ve)
  {
    Real p, dp_dv, dp_de;
    _p_from_v_e_ipol->sampleValueAndDerivatives(v, e, p, dp_dv, dp_de);
    Real T, dT_dv, dT_de;
    _T_from_v_e_ipol->sampleValueAndDerivatives(v, e, T, dT_dv, dT_de);
    Real dk_dp, dk_dT;
    k_from_p_T(p, T, k, dk_dp, dk_dT);
    dk_dv = dk_dp * dp_dv + dk_dT * dT_dv;
    dk_de = dk_dp * dp_de + dk_dT * dT_de;
  }
  else if (_fp)
    _fp->k_from_v_e(v, e, k, dk_dv, dk_de);
  else
    NeedTabulationOrFPError("k_from_v_e with derivatives", "k");
}

◆ makeZeroAndOne() [1/2]

template<>

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

inlineinherited

Definition at line 485 of file SinglePhaseFluidProperties.h.

{
  return {Real{0}, Real{1}};
}

◆ makeZeroAndOne() [2/2]

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.

{
  return {T{0, 0}, T{1, 0}};
}

Referenced by SinglePhaseFluidProperties::xyDerivatives().

◆ missingVEInterpolationError()

void TabulatedFluidProperties::missingVEInterpolationError ( const std::string & function_name ) const

protected

Standardized error message for missing interpolation.

Definition at line 2791 of file TabulatedFluidProperties.C.

{
  mooseError(function_name +
             ": to call this function you must:\n-add this property to the list to the list of "
             "'interpolated_properties'\n and then either:\n-construct (p, T) from (v, e) "
             "tabulations using the 'construct_pT_from_ve' parameter\n-load (v,e) interpolation "
             "tables using the 'fluid_property_ve_file' parameter");
}

Referenced by c_from_v_e(), c_from_v_e(), cp_from_v_e(), cp_from_v_e(), cv_from_v_e(), cv_from_v_e(), g_from_v_e(), k_from_v_e(), k_from_v_e(), mu_from_v_e(), mu_from_v_e(), p_from_v_e(), p_from_v_e(), p_from_v_e(), s_from_v_e(), s_from_v_e(), T_from_v_e(), T_from_v_e(), and T_from_v_e().

◆ molarMass()

Real TabulatedFluidProperties::molarMass ( ) const

overridevirtual

Molar mass [kg/mol].

Returns: molar mass

Reimplemented from SinglePhaseFluidProperties.

Definition at line 388 of file TabulatedFluidProperties.C.

{
  if (_fp)
    return _fp->molarMass();
  else
    TabulationNotImplementedError("molarMass");
}

◆ mu_from_p_T() [1/2]

Real TabulatedFluidProperties::mu_from_p_T	(	Real	pressure,
		Real	temperature
	)		const

overridevirtual

Definition at line 986 of file TabulatedFluidProperties.C.

{
  if (_interpolate_viscosity && _create_direct_pT_interpolations)
  {
    checkInputVariables(pressure, temperature);
    return _property_ipol[_viscosity_idx]->sample(pressure, temperature);
  }
  else
  {
    if (_fp)
      return _fp->mu_from_p_T(pressure, temperature);
    else
      NeedTabulationOrFPError("mu_from_p_T", "viscosity");
  }
}

Referenced by mu_from_v_e(), and mu_from_v_e().

◆ mu_from_p_T() [2/2]

void TabulatedFluidProperties::mu_from_p_T	(	Real	pressure,
		Real	temperature,
		Real &	mu,
		Real &	dmu_dp,
		Real &	dmu_dT
	)		const

overridevirtual

Definition at line 1003 of file TabulatedFluidProperties.C.

{
  if (_interpolate_viscosity && _create_direct_pT_interpolations)
  {
    checkInputVariables(pressure, temperature);
    _property_ipol[_viscosity_idx]->sampleValueAndDerivatives(
        pressure, temperature, mu, dmu_dp, dmu_dT);
  }
  else
  {
    if (_fp)
      _fp->mu_from_p_T(pressure, temperature, mu, dmu_dp, dmu_dT);
    else
      NeedTabulationOrFPError("mu_from_p_T with derivatives", "viscosity");
  }
}

◆ mu_from_v_e() [1/2]

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

overridevirtual

Definition at line 1622 of file TabulatedFluidProperties.C.

{
  if (_interpolate_viscosity && !_construct_pT_from_ve && !_create_direct_ve_interpolations)
    missingVEInterpolationError(__PRETTY_FUNCTION__);
  checkInputVariablesVE(v, e);
 
  if (_create_direct_ve_interpolations && _interpolate_viscosity)
    return _property_ve_ipol[_viscosity_idx]->sample(v, e);
  else if (_construct_pT_from_ve)
  {
    Real p = _p_from_v_e_ipol->sample(v, e);
    Real T = _T_from_v_e_ipol->sample(v, e);
    return mu_from_p_T(p, T);
  }
  else if (_fp)
    return _fp->mu_from_v_e(v, e);
  else
    NeedTabulationOrFPError("mu_from_v_e", "viscosity");
}

Referenced by writeTabulatedData().

◆ mu_from_v_e() [2/2]

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

overridevirtual

Definition at line 1643 of file TabulatedFluidProperties.C.

{
  if (_interpolate_viscosity & !_construct_pT_from_ve && !_create_direct_ve_interpolations)
    missingVEInterpolationError(__PRETTY_FUNCTION__);
  checkInputVariablesVE(v, e);
 
  if (_create_direct_ve_interpolations && _interpolate_viscosity)
    _property_ve_ipol[_viscosity_idx]->sampleValueAndDerivatives(v, e, mu, dmu_dv, dmu_de);
  else if (_construct_pT_from_ve)
  {
    Real p, dp_dv, dp_de;
    _p_from_v_e_ipol->sampleValueAndDerivatives(v, e, p, dp_dv, dp_de);
    Real T, dT_dv, dT_de;
    _T_from_v_e_ipol->sampleValueAndDerivatives(v, e, T, dT_dv, dT_de);
    Real dmu_dp, dmu_dT;
    mu_from_p_T(p, T, mu, dmu_dp, dmu_dT);
    dmu_dv = dmu_dp * dp_dv + dmu_dT * dT_dv;
    dmu_de = dmu_dp * dp_de + dmu_dT * dT_de;
  }
  else if (_fp)
    _fp->mu_from_v_e(v, e, mu, dmu_dv, dmu_de);
  else
    NeedTabulationOrFPError("mu_from_v_e with derivatives", "viscosity");
}

◆ NeedTabulationError()

void TabulatedFluidProperties::NeedTabulationError ( const std::string & needed_property ) const

protected

Utility to forward errors related to properties being requested for tabulation, but no tabulation is present This should generally be used as an 'else' condition to if (_interpolate_needed_property)

Definition at line 1911 of file TabulatedFluidProperties.C.

{
  mooseError("Property '" + needed_property +
             "' is marked as interpolated but neither of the following methods are active:\n- "
             "(p,T) interpolation created from fluid properties ('create_pT_interpolations' "
             "parameter)\n- a (p,T) tabulation file ('fluid_property_file')\n- (v,e) interpolation "
             "created from fluid properties or a (p,T) tabulation ('create_ve_interpolations' "
             "parameter)\n- a (v,e) tabulation file ('fluid_property_ve_file' parameter)");
}

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

◆ NeedTabulationOrFPError()

void TabulatedFluidProperties::NeedTabulationOrFPError	(	const std::string &	desired_routine,
		const std::string &	needed_property
	)		const

protected

Utility to forward errors related to fluid properties needing more data for their computation This should generally be used as an 'else' condition to if (_interpolate_property) / else if (_fp)

Definition at line 1900 of file TabulatedFluidProperties.C.

{
  mooseError(
      "TabulatedFluidProperties can only call the function '" + desired_routine +
      "' when either:\n- the property '" + needed_property +
      "' is tabulated and listed in the 'interpolated_properties' parameter.\n- the 'input_fp' "
      "parameter is provided.");
}

Referenced by c_from_p_T(), c_from_p_T(), c_from_v_e(), c_from_v_e(), cp_from_p_T(), cp_from_p_T(), cp_from_v_e(), cp_from_v_e(), cv_from_p_T(), cv_from_p_T(), cv_from_v_e(), cv_from_v_e(), e_from_p_T(), e_from_p_T(), e_from_p_T(), e_from_v_h(), e_from_v_h(), h_from_p_T(), h_from_p_T(), h_from_p_T(), k_from_p_T(), k_from_p_T(), k_from_v_e(), k_from_v_e(), mu_from_p_T(), mu_from_p_T(), mu_from_v_e(), mu_from_v_e(), p_from_v_e(), p_from_v_e(), p_from_v_e(), rho_from_p_T(), rho_from_p_T(), rho_from_p_T(), rho_from_p_T(), s_from_p_T(), s_from_p_T(), s_from_v_e(), s_from_v_e(), T_from_p_h(), T_from_p_h(), T_from_p_rho(), T_from_p_rho(), T_from_v_e(), T_from_v_e(), T_from_v_e(), v_from_p_T(), v_from_p_T(), and v_from_p_T().

◆ p_from_v_e() [1/3]

void TabulatedFluidProperties::p_from_v_e	(	const ADReal &	v,
		const ADReal &	e,
		ADReal &	p,
		ADReal &	dp_dv,
		ADReal &	dp_de
	)		const

overridevirtual

Definition at line 1409 of file TabulatedFluidProperties.C.

{
  if (_interpolate_pressure && !_construct_pT_from_ve && !_create_direct_ve_interpolations)
    missingVEInterpolationError(__PRETTY_FUNCTION__);
  ADReal vc = v, ec = e;
  checkInputVariablesVE(vc, ec);
 
  if (_create_direct_ve_interpolations && _interpolate_pressure)
    _property_ve_ipol[_p_idx]->sampleValueAndDerivatives(vc, ec, p, dp_dv, dp_de);
  else if (_construct_pT_from_ve)
    _p_from_v_e_ipol->sampleValueAndDerivatives(vc, ec, p, dp_dv, dp_de);
  else if (_fp)
    _fp->p_from_v_e(vc, ec, p, dp_dv, dp_de);
  else
    NeedTabulationOrFPError("AD p_from_v_e with derivatives", "pressure");
}

◆ p_from_v_e() [2/3]

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

overridevirtual

Derivatives like dc_dv & dc_de are computed using the chain rule dy/dx(p,T) = dy/dp * dp/dx + dy/dT * dT/dx where y = c, cp, cv... & x = v, e.

Definition at line 1375 of file TabulatedFluidProperties.C.

{
  if (_interpolate_pressure && !_construct_pT_from_ve && !_create_direct_ve_interpolations)
    missingVEInterpolationError(__PRETTY_FUNCTION__);
  checkInputVariablesVE(v, e);
 
  if (_create_direct_ve_interpolations && _interpolate_pressure)
    return _property_ve_ipol[_p_idx]->sample(v, e);
  else if (_construct_pT_from_ve)
    return _p_from_v_e_ipol->sample(v, e);
  else if (_fp)
    return _fp->p_from_v_e(v, e);
  else
    NeedTabulationOrFPError("p_from_v_e", "pressure");
}

Referenced by TabulatedBicubicFluidProperties::constructInterpolation(), e_from_p_rho(), e_from_p_rho(), v_from_p_T(), v_from_p_T(), and writeTabulatedData().

◆ p_from_v_e() [3/3]

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

overridevirtual

Definition at line 1392 of file TabulatedFluidProperties.C.

{
  if (_interpolate_pressure && !_construct_pT_from_ve && !_create_direct_ve_interpolations)
    missingVEInterpolationError(__PRETTY_FUNCTION__);
  checkInputVariablesVE(v, e);
 
  if (_create_direct_ve_interpolations && _interpolate_pressure)
    _property_ve_ipol[_p_idx]->sampleValueAndDerivatives(v, e, p, dp_dv, dp_de);
  else if (_construct_pT_from_ve)
    _p_from_v_e_ipol->sampleValueAndDerivatives(v, e, p, dp_dv, dp_de);
  else if (_fp)
    _fp->p_from_v_e(v, e, p, dp_dv, dp_de);
  else
    NeedTabulationOrFPError("p_from_v_e with derivatives", "pressure");
}

◆ 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.

{
  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"));
}

Referenced by T_from_h_s().

◆ 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.

{
  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"));
}

Referenced by TabulatedBicubicFluidProperties::constructInterpolation(), TemperaturePressureFunctionFluidProperties::cp_from_v_e(), TemperaturePressureFunctionFluidProperties::cv_from_v_e(), TemperaturePressureFunctionFluidProperties::cv_from_v_e(), g_from_v_e(), TemperaturePressureFunctionFluidProperties::k_from_v_e(), TemperaturePressureFunctionFluidProperties::mu_from_v_e(), and TemperaturePressureFunctionFluidProperties::T_from_v_e().

◆ 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.

{
  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"));
}

Referenced by TabulatedBicubicFluidProperties::constructInterpolation().

◆ propfunc() [1/12]

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

inherited

◆ propfunc() [2/12]

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

inherited

◆ propfunc() [3/12]

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

inherited

◆ propfunc() [4/12]

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

inherited

◆ propfunc() [5/12]

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

inherited

◆ propfunc() [6/12]

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

inherited

◆ propfunc() [7/12]

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

inherited

◆ propfunc() [8/12]

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

inherited

◆ propfunc() [9/12]

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:

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

As an example:

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

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

Automatic differentiation (AD) support is provided through x_from_a_b(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:

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

◆ propfunc() [10/12]

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

inherited

◆ propfunc() [11/12]

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

inherited

◆ propfunc() [12/12]

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

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

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 SinglePhaseFluidProperties::propfuncWithDefault	(	mu	,
		p	,
		T
	)

inherited

◆ propfuncWithDefault() [5/7]

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

inherited

◆ propfuncWithDefault() [6/7]

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

inherited

◆ propfuncWithDefault() [7/7]

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

inherited

◆ readFileTabulationData()

void TabulatedFluidProperties::readFileTabulationData ( bool use_pT )

protected

Read tabulation data from file.

Definition at line 2335 of file TabulatedFluidProperties.C.

{
  std::string file_name;
  if (use_pT)
  {
    _console << name() + ": Reading tabulated properties from " << _file_name_in << std::endl;
    _csv_reader.read();
    file_name = _file_name_in;
  }
  else
  {
    _console << name() + ": Reading tabulated properties from " << _file_name_ve_in << std::endl;
    _csv_reader.setFileName(_file_name_ve_in);
    _csv_reader.read();
    file_name = _file_name_ve_in;
  }
 
  const std::vector<std::string> & column_names = _csv_reader.getNames();
 
  // These columns form the grid and must be present in the file
  std::vector<std::string> required_columns;
  if (use_pT)
    required_columns = {"pressure", "temperature"};
  else
    required_columns = {"specific_volume", "internal_energy"};
 
  // Check that all required columns are present
  for (std::size_t i = 0; i < required_columns.size(); ++i)
  {
    if (std::find(column_names.begin(), column_names.end(), required_columns[i]) ==
        column_names.end())
      mooseError("No ",
                 required_columns[i],
                 " data read in ",
                 file_name,
                 ". A column named ",
                 required_columns[i],
                 " must be present");
  }
 
  // These columns can be present in the file
  std::vector<std::string> property_columns = {
      "density", "enthalpy", "viscosity", "k", "c", "cv", "cp", "entropy"};
  if (use_pT)
    property_columns.push_back("internal_energy");
  else
  {
    property_columns.push_back("pressure");
    property_columns.push_back("temperature");
  }
 
  // Check that any property names read from the file are present in the list of possible
  // properties, and if they are, add them to the list of read properties
  for (std::size_t i = 0; i < column_names.size(); ++i)
  {
    // Only check properties not in _required_columns
    if (std::find(required_columns.begin(), required_columns.end(), column_names[i]) ==
        required_columns.end())
    {
      if (std::find(property_columns.begin(), property_columns.end(), column_names[i]) ==
          property_columns.end())
        mooseWarning(column_names[i],
                     " read in ",
                     file_name,
                     " tabulation file is not one of the properties that TabulatedFluidProperties "
                     "understands. It will be ignored.");
      // We could be reading a (v,e) tabulation after having read a (p,T) tabulation, do not
      // insert twice
      // Also only allow properties specified as interpolated if user passed the parameter
      else if (std::find(_interpolated_properties.begin(),
                         _interpolated_properties.end(),
                         column_names[i]) == _interpolated_properties.end() &&
               (!isParamSetByUser("interpolated_properties") ||
                _interpolated_properties_enum.contains(column_names[i])))
        _interpolated_properties.push_back(column_names[i]);
    }
  }
 
  std::map<std::string, unsigned int> data_index;
  for (std::size_t i = 0; i < column_names.size(); ++i)
  {
    auto it = std::find(column_names.begin(), column_names.end(), column_names[i]);
    data_index[column_names[i]] = std::distance(column_names.begin(), it);
  }
 
  const std::vector<std::vector<Real>> & column_data = _csv_reader.getData();
 
  // Extract the pressure and temperature data vectors
  if (use_pT)
  {
    _pressure = column_data[data_index.find("pressure")->second];
    _temperature = column_data[data_index.find("temperature")->second];
  }
  else
  {
    _specific_volume = column_data[data_index.find("specific_volume")->second];
    _internal_energy = column_data[data_index.find("internal_energy")->second];
  }
 
  if (use_pT)
    checkFileTabulationGrids(_pressure, _temperature, file_name, "pressure", "temperature");
  else
    checkFileTabulationGrids(_specific_volume,
                             _internal_energy,
                             file_name,
                             "specific volume",
                             "specific internal energy");
 
  if (use_pT)
  {
    _num_p = _pressure.size();
    _num_T = _temperature.size();
 
    // Minimum and maximum pressure and temperature. Note that _pressure and
    // _temperature are sorted
    _pressure_min = _pressure.front();
    _pressure_max = _pressure.back();
    _temperature_min = _temperature.front();
    _temperature_max = _temperature.back();
    checkInitialGuess(true);
 
    // Extract the fluid property data from the file
    for (std::size_t i = 0; i < _interpolated_properties.size(); ++i)
      _properties.push_back(column_data[data_index.find(_interpolated_properties[i])->second]);
  }
  else
  {
    _num_v = _specific_volume.size();
    _num_e = _internal_energy.size();
 
    // Minimum and maximum specific internal energy and specific volume
    _v_min = _specific_volume.front();
    _v_max = _specific_volume.back();
    _e_min = _internal_energy.front();
    _e_max = _internal_energy.back();
 
    // We cannot overwrite the tabulated data grid with a grid generated from user-input for the
    // purpose of creating (p,T) to (v,e) interpolations
    if (_construct_pT_from_ve)
      paramError("construct_pT_from_ve",
                 "Reading a (v,e) tabulation and generating (p,T) to (v,e) interpolation tables is "
                 "not supported at this time.");
 
    // Make sure we use the tabulation bounds
    _e_bounds_specified = true;
    _v_bounds_specified = true;
 
    // Extract the fluid property data from the file
    _properties_ve.reserve(_interpolated_properties.size());
    for (std::size_t i = 0; i < _interpolated_properties.size(); ++i)
      _properties_ve.push_back(column_data[data_index.find(_interpolated_properties[i])->second]);
 
    // Obtain the min/max T, p and check the initial guess
    const auto & p_col = column_data[data_index.find("pressure")->second];
    _pressure_min = *std::min_element(p_col.begin(), p_col.end());
    _pressure_max = *std::max_element(p_col.begin(), p_col.end());
    const auto & T_col = column_data[data_index.find("temperature")->second];
    _temperature_min = *std::min_element(T_col.begin(), T_col.end());
    _temperature_max = *std::max_element(T_col.begin(), T_col.end());
    checkInitialGuess(true);
  }
}

Referenced by initialSetup().

◆ 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_s() [1/2]

Real TabulatedFluidProperties::rho_from_p_s	(	Real	p,
		Real	s
	)		const

overridevirtual

Definition at line 592 of file TabulatedFluidProperties.C.

{
  Real T = T_from_p_s(p, s);
  return rho_from_p_T(p, T);
}

◆ rho_from_p_s() [2/2]

void TabulatedFluidProperties::rho_from_p_s	(	Real	p,
		Real	s,
		Real &	rho,
		Real &	drho_dp,
		Real &	drho_ds
	)		const

overridevirtual

Definition at line 599 of file TabulatedFluidProperties.C.

{
  Real T, dT_dp, dT_ds;
  T_from_p_s(p, s, T, dT_dp, dT_ds);
  Real drho_dp_T, drho_dT;
  rho_from_p_T(p, T, rho, drho_dp_T, drho_dT);
  drho_dp = drho_dT * dT_dp + drho_dp_T;
  drho_ds = drho_dT * dT_ds;
}

◆ rho_from_p_T() [1/4]

ADReal TabulatedFluidProperties::rho_from_p_T	(	const ADReal &	pressure,
		const ADReal &	temperature
	)		const

overridevirtual

Definition at line 522 of file TabulatedFluidProperties.C.

{
  if (_interpolate_density && _create_direct_pT_interpolations)
  {
    ADReal pressure_nc = pressure, temperature_nc = temperature;
    checkInputVariables(pressure_nc, temperature_nc);
    return _property_ipol[_density_idx]->sample(pressure_nc, temperature_nc);
  }
  else if (_create_direct_ve_interpolations)
    return 1. / v_from_p_T(pressure, temperature);
  else
  {
    if (_fp)
      return _fp->rho_from_p_T(pressure, temperature);
    else
      NeedTabulationOrFPError("AD rho_from_p_T", "density");
  }
}

◆ rho_from_p_T() [2/4]

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

overridevirtual

Definition at line 570 of file TabulatedFluidProperties.C.

{
  if (_interpolate_density && _create_direct_pT_interpolations)
  {
    ADReal p = pressure, T = temperature;
    checkInputVariables(p, T);
    _property_ipol[_density_idx]->sampleValueAndDerivatives(p, T, rho, drho_dp, drho_dT);
  }
  else
  {
    if (_fp)
      _fp->rho_from_p_T(pressure, temperature, rho, drho_dp, drho_dT);
    else
      NeedTabulationOrFPError("AD rho_from_p_T with derivatives", "density");
  }
}

◆ rho_from_p_T() [3/4]

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

overridevirtual

Definition at line 503 of file TabulatedFluidProperties.C.

{
  if (_interpolate_density && _create_direct_pT_interpolations)
  {
    checkInputVariables(pressure, temperature);
    return _property_ipol[_density_idx]->sample(pressure, temperature);
  }
  else if (_create_direct_ve_interpolations)
    return 1. / v_from_p_T(pressure, temperature);
  else
  {
    if (_fp)
      return _fp->rho_from_p_T(pressure, temperature);
    else
      NeedTabulationOrFPError("rho_from_p_T", "density");
  }
}

Referenced by e_from_p_rho(), e_from_p_T(), e_from_p_T(), rho_from_p_s(), rho_from_p_s(), rho_from_p_T(), T_from_p_rho(), and T_from_p_rho().

◆ rho_from_p_T() [4/4]

void TabulatedFluidProperties::rho_from_p_T	(	Real	pressure,
		Real	temperature,
		Real &	rho,
		Real &	drho_dp,
		Real &	drho_dT
	)		const

overridevirtual

Definition at line 542 of file TabulatedFluidProperties.C.

{
  if (_interpolate_density && _create_direct_pT_interpolations)
  {
    checkInputVariables(pressure, temperature);
    _property_ipol[_density_idx]->sampleValueAndDerivatives(
        pressure, temperature, rho, drho_dp, drho_dT);
  }
  else if (_create_direct_ve_interpolations)
  {
    checkInputVariables(pressure, temperature);
    // use finite differencing stencil
    rho = rho_from_p_T(pressure, temperature);
    Real eps = 1e-8;
    drho_dp = (rho_from_p_T(pressure * (1 + eps), temperature) - rho) / (eps * pressure);
    drho_dT = (rho_from_p_T(pressure, temperature * (1 + eps)) - rho) / (eps * temperature);
  }
  else
  {
    if (_fp)
      _fp->rho_from_p_T(pressure, temperature, rho, drho_dp, drho_dT);
    else
      NeedTabulationOrFPError("rho_from_p_T with derivatives", "density");
  }
}

◆ rho_mu_from_p_T() [1/3]

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);
}

◆ 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 CO2FluidProperties, HydrogenFluidProperties, NitrogenFluidProperties, and Water97FluidProperties.

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	(	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 CO2FluidProperties, HydrogenFluidProperties, NitrogenFluidProperties, and Water97FluidProperties.

Definition at line 452 of file SinglePhaseFluidProperties.C.

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

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

◆ s_from_h_p() [1/2]

Real TabulatedFluidProperties::s_from_h_p	(	Real	h,
		Real	pressure
	)		const

overridevirtual

Definition at line 1874 of file TabulatedFluidProperties.C.

{
  Real T = T_from_p_h(pressure, enthalpy);
  return s_from_p_T(pressure, T);
}

◆ s_from_h_p() [2/2]

void TabulatedFluidProperties::s_from_h_p	(	Real	h,
		Real	pressure,
		Real &	s,
		Real &	ds_dh,
		Real &	ds_dp
	)		const

overridevirtual

Definition at line 1881 of file TabulatedFluidProperties.C.

{
  if (_fp)
    _fp->s_from_h_p(h, pressure, s, ds_dh, ds_dp);
  else
    TabulationNotImplementedError("s_from_h_p with derivatives");
}

◆ s_from_p_T() [1/2]

void TabulatedFluidProperties::s_from_p_T	(	Real	p,
		Real	T,
		Real &	s,
		Real &	ds_dp,
		Real &	ds_dT
	)		const

overridevirtual

Definition at line 1180 of file TabulatedFluidProperties.C.

{
  if (_interpolate_entropy)
  {
    checkInputVariables(p, T);
    if (_create_direct_pT_interpolations)
      _property_ipol[_entropy_idx]->sampleValueAndDerivatives(p, T, s, ds_dp, ds_dT);
    else if (_create_direct_ve_interpolations)
    {
      Real v, e, dv_dp, dv_dT, de_dp, de_dT;
      SinglePhaseFluidProperties::v_e_from_p_T(p, T, v, dv_dp, dv_dT, e, de_dp, de_dT);
      Real ds_dv, ds_de;
      _property_ve_ipol[_entropy_idx]->sampleValueAndDerivatives(v, e, s, ds_dv, ds_de);
      ds_dp = ds_dv * dv_dp + ds_de * de_dp;
      ds_dT = ds_dv * dv_dT + ds_de * de_dT;
    }
    else
      NeedTabulationError("entropy");
  }
  else
  {
    if (_fp)
      _fp->s_from_p_T(p, T, s, ds_dp, ds_dT);
    else
      NeedTabulationOrFPError("s_from_p_T with derivatives", "entropy");
  }
}

◆ s_from_p_T() [2/2]

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

overridevirtual

Definition at line 1163 of file TabulatedFluidProperties.C.

{
  if (_interpolate_entropy && _create_direct_pT_interpolations)
  {
    checkInputVariables(pressure, temperature);
    return _property_ipol[_entropy_idx]->sample(pressure, temperature);
  }
  else
  {
    if (_fp)
      return _fp->s_from_p_T(pressure, temperature);
    else
      NeedTabulationOrFPError("s_from_p_T", "entropy");
  }
}

Referenced by g_from_v_e(), s_from_h_p(), s_from_v_e(), s_from_v_e(), and T_from_p_s().

◆ s_from_v_e() [1/2]

Real TabulatedFluidProperties::s_from_v_e	(	Real	v,
		Real	e
	)		const

overridevirtual

Definition at line 1716 of file TabulatedFluidProperties.C.

{
  if (_interpolate_entropy && !_construct_pT_from_ve && !_create_direct_ve_interpolations)
    missingVEInterpolationError(__PRETTY_FUNCTION__);
  checkInputVariablesVE(v, e);
 
  if (_create_direct_ve_interpolations && _interpolate_entropy)
    return _property_ve_ipol[_entropy_idx]->sample(v, e);
  else if (_construct_pT_from_ve)
  {
    Real T = _T_from_v_e_ipol->sample(v, e);
    Real p = _p_from_v_e_ipol->sample(v, e);
    return s_from_p_T(p, T);
  }
  else if (_fp)
    return _fp->s_from_v_e(v, e);
  else
    NeedTabulationOrFPError("s_from_v_e", "entropy");
}

Referenced by writeTabulatedData().

◆ s_from_v_e() [2/2]

void TabulatedFluidProperties::s_from_v_e	(	Real	v,
		Real	e,
		Real &	s,
		Real &	ds_dv,
		Real &	ds_de
	)		const

overridevirtual

Definition at line 1737 of file TabulatedFluidProperties.C.

{
  if (_interpolate_entropy && !_construct_pT_from_ve && !_create_direct_ve_interpolations)
    missingVEInterpolationError(__PRETTY_FUNCTION__);
  checkInputVariablesVE(v, e);
 
  if (_create_direct_ve_interpolations && _interpolate_entropy)
    _property_ve_ipol[_entropy_idx]->sampleValueAndDerivatives(v, e, s, ds_dv, ds_de);
  else if (_construct_pT_from_ve)
  {
    Real p, T, dT_dv, dT_de, dp_dv, dp_de;
    _T_from_v_e_ipol->sampleValueAndDerivatives(v, e, T, dT_dv, dT_de);
    _p_from_v_e_ipol->sampleValueAndDerivatives(v, e, p, dp_dv, dp_de);
    Real ds_dp, ds_dT;
    s_from_p_T(p, T, s, ds_dp, ds_dT);
    ds_dv = ds_dp * dp_dv + ds_dT * dT_dv;
    ds_dv = ds_dp * dp_de + ds_dT * dT_de;
  }
  else if (_fp)
    _fp->s_from_v_e(v, e, s, ds_dv, ds_de);
  else
    NeedTabulationOrFPError("s_from_v_e", "entropy");
}

◆ subdomainSetup()

virtual void FluidProperties::subdomainSetup ( )

inlinefinalvirtualinherited

Reimplemented from ThreadedGeneralUserObject.

Definition at line 38 of file FluidProperties.h.

38{}

◆ T_from_h_s()

Real TabulatedFluidProperties::T_from_h_s	(	Real	h,
		Real	s
	)		const

virtual

Definition at line 1794 of file TabulatedFluidProperties.C.

{
  Real p0 = _p_initial_guess;
  Real T0 = _T_initial_guess;
  Real p, T;
  bool conversion_succeeded;
  p_T_from_h_s(h, s, p0, T0, p, T, conversion_succeeded);
  return T;
}

◆ T_from_p_h() [1/2]

ADReal TabulatedFluidProperties::T_from_p_h	(	const ADReal &	pressure,
		const ADReal &	enthalpy
	)		const

overridevirtual

Definition at line 1836 of file TabulatedFluidProperties.C.

{
  using std::isnan;
  if (_create_direct_pT_interpolations || _create_direct_ve_interpolations)
  {
    auto lambda =
        [&](ADReal pressure, ADReal current_T, ADReal & new_h, ADReal & dh_dp, ADReal & dh_dT)
    {
      h_from_p_T(pressure.value(), current_T.value(), new_h.value(), dh_dp.value(), dh_dT.value());
      // Reconstruct derivatives
      new_h.derivatives() =
          dh_dp.value() * pressure.derivatives() + dh_dT.value() * current_T.derivatives();
    };
    ADReal T = FluidPropertiesUtils::NewtonSolve(pressure,
                                                 enthalpy,
                                                 _T_initial_guess,
                                                 _tolerance,
                                                 lambda,
                                                 name() + "::T_from_p_h",
                                                 _max_newton_its,
                                                 _verbose_newton)
                   .first;
    // check for nans
    if (isnan(T))
      mooseError("Conversion from enthalpy (h = ",
                 enthalpy,
                 ") and pressure (p = ",
                 pressure,
                 ") to temperature failed to converge.");
    return T;
  }
  else if (_fp)
    return _fp->T_from_p_h(pressure, enthalpy);
  else
    NeedTabulationOrFPError("T_from_p_h", "temperature");
}

◆ T_from_p_h() [2/2]

Real TabulatedFluidProperties::T_from_p_h	(	Real	pressure,
		Real	enthalpy
	)		const

overridevirtual

Definition at line 1805 of file TabulatedFluidProperties.C.

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

Referenced by s_from_h_p().

◆ T_from_p_rho() [1/3]

ADReal TabulatedFluidProperties::T_from_p_rho	(	const ADReal &	pressure,
		const ADReal &	rho
	)		const

virtual

Definition at line 828 of file TabulatedFluidProperties.C.

{
  if (_interpolate_density)
  {
    auto lambda =
        [&](ADReal p, ADReal current_T, ADReal & new_rho, ADReal & drho_dp, ADReal & drho_dT)
    { rho_from_p_T(p, current_T, new_rho, drho_dp, drho_dT); };
    ADReal T = FluidPropertiesUtils::NewtonSolve(pressure,
                                                 rho,
                                                 _T_initial_guess,
                                                 _tolerance,
                                                 lambda,
                                                 name() + "::T_from_p_rho",
                                                 _max_newton_its,
                                                 _verbose_newton)
                   .first;
    // check for nans
    if (std::isnan(T.value()))
      mooseError("Conversion from pressure (p = ",
                 pressure,
                 ") and density (rho = ",
                 rho,
                 ") to temperature failed to converge.");
    return T;
  }
  else if (_create_direct_ve_interpolations)
    return T_from_v_e(1. / rho, e_from_p_rho(pressure, rho));
  else
    NeedTabulationOrFPError("AD T_from_p_rho", "temperature");
}

◆ T_from_p_rho() [2/3]

Real TabulatedFluidProperties::T_from_p_rho	(	Real	pressure,
		Real	rho
	)		const

virtual

Definition at line 795 of file TabulatedFluidProperties.C.

{
  Real T = _T_initial_guess;
  if (_interpolate_density && _create_direct_pT_interpolations)
  {
    checkInputVariables(pressure, T);
    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); };
    T = FluidPropertiesUtils::NewtonSolve(pressure,
                                          rho,
                                          _T_initial_guess,
                                          _tolerance,
                                          lambda,
                                          name() + "::T_from_p_rho",
                                          _max_newton_its,
                                          _verbose_newton)
            .first;
  }
  else if (_create_direct_ve_interpolations)
    T = T_from_v_e(1. / rho, e_from_p_rho(pressure, rho));
  else
    NeedTabulationOrFPError("T_from_p_rho", "temperature");
  // check for nans
  if (std::isnan(T))
    mooseError("Conversion from pressure (p = ",
               pressure,
               ") and density (rho = ",
               rho,
               ") to temperature failed to converge.");
  return T;
}

Referenced by e_from_p_rho(), e_from_p_rho(), e_from_p_rho(), and T_from_p_rho().

◆ T_from_p_rho() [3/3]

void TabulatedFluidProperties::T_from_p_rho	(	Real	pressure,
		Real	rho,
		Real &	T,
		Real &	dT_dp,
		Real &	dT_drho
	)		const

virtual

Definition at line 860 of file TabulatedFluidProperties.C.

{
  T = T_from_p_rho(pressure, rho);
  Real eps = 1e-8;
  dT_dp = (T_from_p_rho(pressure * (1 + eps), rho) - T) / (eps * pressure);
  dT_drho = (T_from_p_rho(pressure, rho * (1 + eps)) - T) / (eps * rho);
}

◆ T_from_p_s() [1/2]

Real TabulatedFluidProperties::T_from_p_s	(	Real	p,
		Real	s
	)		const

virtual

Definition at line 870 of file TabulatedFluidProperties.C.

{
  auto lambda = [&](Real p, Real current_T, Real & new_s, Real & ds_dp, Real & ds_dT)
  { s_from_p_T(p, current_T, new_s, ds_dp, ds_dT); };
  Real T = FluidPropertiesUtils::NewtonSolve(pressure,
                                             s,
                                             _T_initial_guess,
                                             _tolerance,
                                             lambda,
                                             name() + "::T_from_p_s",
                                             _max_newton_its,
                                             _verbose_newton)
               .first;
  // check for nans
  if (std::isnan(T))
    mooseError("Conversion from pressure (p = ",
               pressure,
               ") and entropy (s = ",
               s,
               ") to temperature failed to converge.");
  return T;
}

Referenced by rho_from_p_s(), rho_from_p_s(), and T_from_p_s().

◆ T_from_p_s() [2/2]

void TabulatedFluidProperties::T_from_p_s	(	Real	p,
		Real	s,
		Real &	T,
		Real &	dT_dp,
		Real &	dT_ds
	)		const

virtual

Definition at line 894 of file TabulatedFluidProperties.C.

{
  T = T_from_p_s(pressure, s);
  Real eps = 1e-8;
  dT_dp = (T_from_p_s(pressure * (1 + eps), s) - T) / (eps * pressure);
  dT_ds = (T_from_p_s(pressure, s * (1 + eps)) - T) / (eps * s);
}

◆ T_from_v_e() [1/3]

void TabulatedFluidProperties::T_from_v_e	(	const ADReal &	v,
		const ADReal &	e,
		ADReal &	p,
		ADReal &	dp_dv,
		ADReal &	dp_de
	)		const

overridevirtual

Definition at line 1462 of file TabulatedFluidProperties.C.

{
  if (_interpolate_temperature && !_construct_pT_from_ve && !_create_direct_ve_interpolations)
    missingVEInterpolationError(__PRETTY_FUNCTION__);
  ADReal vc = v, ec = e;
  checkInputVariablesVE(vc, ec);
 
  if (_create_direct_ve_interpolations && _interpolate_temperature)
    _property_ve_ipol[_T_idx]->sampleValueAndDerivatives(vc, ec, T, dT_dv, dT_de);
  else if (_construct_pT_from_ve)
    _T_from_v_e_ipol->sampleValueAndDerivatives(vc, ec, T, dT_dv, dT_de);
  else if (_fp)
    _fp->T_from_v_e(vc, ec, T, dT_dv, dT_de);
  else
    NeedTabulationOrFPError("AD T_from_v_e with derivatives", "temperature");
}

◆ T_from_v_e() [2/3]

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

overridevirtual

Definition at line 1428 of file TabulatedFluidProperties.C.

{
  if (_interpolate_temperature && !_construct_pT_from_ve && !_create_direct_ve_interpolations)
    missingVEInterpolationError(__PRETTY_FUNCTION__);
  checkInputVariablesVE(v, e);
 
  if (_create_direct_ve_interpolations && _interpolate_temperature)
    return _property_ve_ipol[_T_idx]->sample(v, e);
  else if (_construct_pT_from_ve)
    return _T_from_v_e_ipol->sample(v, e);
  else if (_fp)
    return _fp->T_from_v_e(v, e);
  else
    NeedTabulationOrFPError("T_from_v_e", "temperature");
}

Referenced by TabulatedBicubicFluidProperties::constructInterpolation(), e_from_p_T(), e_from_p_T(), T_from_p_rho(), T_from_p_rho(), v_from_p_T(), v_from_p_T(), and writeTabulatedData().

◆ T_from_v_e() [3/3]

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

overridevirtual

Definition at line 1445 of file TabulatedFluidProperties.C.

{
  if (_interpolate_temperature && !_construct_pT_from_ve && !_create_direct_ve_interpolations)
    missingVEInterpolationError(__PRETTY_FUNCTION__);
  checkInputVariablesVE(v, e);
 
  if (_create_direct_ve_interpolations && _interpolate_temperature)
    _property_ve_ipol[_T_idx]->sampleValueAndDerivatives(v, e, T, dT_dv, dT_de);
  else if (_construct_pT_from_ve)
    _T_from_v_e_ipol->sampleValueAndDerivatives(v, e, T, dT_dv, dT_de);
  else if (_fp)
    _fp->T_from_v_e(v, e, T, dT_dv, dT_de);
  else
    NeedTabulationOrFPError("T_from_v_e with derivatives", "temperature");
}

◆ TabulationNotImplementedError()

void TabulatedFluidProperties::TabulationNotImplementedError ( const std::string & desired_routine ) const

protected

Utility to forward errors related to fluid properties methods not implemented.

Definition at line 1891 of file TabulatedFluidProperties.C.

{
  mooseError("TabulatedFluidProperties can only call the function '" + desired_routine +
             "' when the 'input_fp' parameter is provided. It is currently not implemented using "
             "tabulations, and this property is simply forwarded to the FluidProperties specified "
             "in the 'input_fp' parameter");
}

Referenced by criticalDensity(), criticalPressure(), criticalTemperature(), henryCoefficients(), molarMass(), s_from_h_p(), triplePointPressure(), triplePointTemperature(), vaporPressure(), vaporPressure(), vaporTemperature(), and vaporTemperature().

◆ threadJoin()

virtual void FluidProperties::threadJoin ( const UserObject & )

inlinefinalvirtualinherited

Reimplemented from ThreadedGeneralUserObject.

Definition at line 37 of file FluidProperties.h.

37{}

◆ triplePointPressure()

Real TabulatedFluidProperties::triplePointPressure ( ) const

overridevirtual

Triple point pressure.

Returns: triple point pressure (Pa)

Reimplemented from SinglePhaseFluidProperties.

Definition at line 1326 of file TabulatedFluidProperties.C.

{
 
  if (_fp)
    return _fp->triplePointPressure();
  else
    TabulationNotImplementedError("triplePointPressure");
}

◆ triplePointTemperature()

Real TabulatedFluidProperties::triplePointTemperature ( ) const

overridevirtual

Triple point temperature.

Returns: triple point temperature (K)

Reimplemented from SinglePhaseFluidProperties.

Definition at line 1336 of file TabulatedFluidProperties.C.

{
 
  if (_fp)
    return _fp->triplePointTemperature();
  else
    TabulationNotImplementedError("triplePointTemperature");
}

◆ unimplementedDerivativeMethod()

void SinglePhaseFluidProperties::unimplementedDerivativeMethod ( const std::string & property_function_name ) const

inlineprivateinherited

Definition at line 454 of file SinglePhaseFluidProperties.h.

  {
    const std::string message =
        "The fluid properties class '" + type() +
        "' has not implemented the method below, which computes derivatives of fluid properties "
        "with regards to the flow variables. If your application requires this "
        "method, you must either implement it or use a different fluid properties "
        " class.\n\n" +
        property_function_name;
 
    if (_allow_imperfect_jacobians)
      mooseDoOnce(mooseWarning(message + "\nThe unimplemented derivatives for this fluid property "
                                         "are currently neglected, set to 0."));
    else
      mooseError(message + "\n\nYou can avoid this error by neglecting the "
                           "unimplemented derivatives of fluid properties by setting the "
                           "'allow_imperfect_jacobians' parameter");
  }

Referenced by SinglePhaseFluidProperties::vaporPressure(), and SinglePhaseFluidProperties::vaporTemperature().

◆ 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 &	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_from_p_T() [2/2]

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.

{
  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);
  }
}

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

◆ 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 CaloricallyImperfectGas, IdealGasFluidProperties, and StiffenedGasFluidProperties.

Definition at line 489 of file SinglePhaseFluidProperties.C.

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

◆ v_from_p_T() [1/3]

ADReal TabulatedFluidProperties::v_from_p_T	(	const ADReal &	pressure,
		const ADReal &	temperature
	)		const

overridevirtual

Definition at line 437 of file TabulatedFluidProperties.C.

{
  if (_interpolate_density && _create_direct_pT_interpolations)
  {
    ADReal pressure_nc = pressure, temperature_nc = temperature;
    checkInputVariables(pressure_nc, temperature_nc);
    return 1.0 / _property_ipol[_density_idx]->sample(pressure_nc, temperature_nc);
  }
  else if (_create_direct_ve_interpolations)
  {
    ADReal pressure_nc = pressure, temperature_nc = temperature;
    checkInputVariables(pressure_nc, temperature_nc);
    ADReal v, e;
    auto p_from_v_e = [&](ADReal v, ADReal e, ADReal & new_p, ADReal & dp_dv, ADReal & dp_de)
    { this->p_from_v_e(v, e, new_p, dp_dv, dp_de); };
    auto T_from_v_e = [&](ADReal v, ADReal e, ADReal & new_T, ADReal & dT_dv, ADReal & dT_de)
    { this->T_from_v_e(v, e, new_T, dT_dv, dT_de); };
    FluidPropertiesUtils::NewtonSolve2D(pressure_nc,
                                        temperature_nc,
                                        (_v_min + _v_max) / 2,
                                        (_e_min + _e_max) / 2,
                                        v,
                                        e,
                                        _tolerance,
                                        _tolerance,
                                        p_from_v_e,
                                        T_from_v_e,
                                        name() + "::v_from_p_T",
                                        _max_newton_its,
                                        _verbose_newton);
    return v;
  }
  else
  {
    if (_fp)
      return 1.0 / _fp->rho_from_p_T(pressure, temperature);
    else
      NeedTabulationOrFPError("AD v_from_p_T", "density");
  }
}

◆ v_from_p_T() [2/3]

Real TabulatedFluidProperties::v_from_p_T	(	Real	pressure,
		Real	temperature
	)		const

overridevirtual

Definition at line 397 of file TabulatedFluidProperties.C.

{
  if (_interpolate_density && _create_direct_pT_interpolations)
  {
    checkInputVariables(pressure, temperature);
    return 1.0 / _property_ipol[_density_idx]->sample(pressure, temperature);
  }
  else if (_create_direct_ve_interpolations)
  {
    checkInputVariables(pressure, temperature);
    Real v, e;
    auto p_from_v_e = [&](Real v, Real e, Real & new_p, Real & dp_dv, Real & dp_de)
    { this->p_from_v_e(v, e, new_p, dp_dv, dp_de); };
    auto T_from_v_e = [&](Real v, Real e, Real & new_T, Real & dT_dv, Real & dT_de)
    { this->T_from_v_e(v, e, new_T, dT_dv, dT_de); };
    FluidPropertiesUtils::NewtonSolve2D(pressure,
                                        temperature,
                                        (_v_min + _v_max) / 2,
                                        (_e_min + _e_max) / 2,
                                        v,
                                        e,
                                        _tolerance,
                                        _tolerance,
                                        p_from_v_e,
                                        T_from_v_e,
                                        name() + "::v_from_p_T",
                                        _max_newton_its,
                                        _verbose_newton);
    return v;
  }
  else
  {
    if (_fp)
      return 1.0 / _fp->rho_from_p_T(pressure, temperature);
    else
      NeedTabulationOrFPError("AD v_from_p_T", "density");
  }
}

Referenced by rho_from_p_T(), and rho_from_p_T().

◆ v_from_p_T() [3/3]

void TabulatedFluidProperties::v_from_p_T	(	Real	pressure,
		Real	temperature,
		Real &	v,
		Real &	dv_dp,
		Real &	dv_dT
	)		const

overridevirtual

Definition at line 479 of file TabulatedFluidProperties.C.

{
  Real rho = 0, drho_dp = 0, drho_dT = 0;
  if (_interpolate_density && _create_direct_pT_interpolations)
  {
    checkInputVariables(pressure, temperature);
    _property_ipol[_density_idx]->sampleValueAndDerivatives(
        pressure, temperature, rho, drho_dp, drho_dT);
  }
  else
  {
    if (_fp)
      _fp->rho_from_p_T(pressure, temperature, rho, drho_dp, drho_dT);
    else
      NeedTabulationOrFPError("v_from_p_T with derivatives", "density");
  }
  // convert from rho to v
  v = 1.0 / rho;
  dv_dp = -drho_dp / (rho * rho);
  dv_dT = -drho_dT / (rho * rho);
}

◆ validParams()

InputParameters TabulatedFluidProperties::validParams ( )

static

Definition at line 24 of file TabulatedFluidProperties.C.

{
  InputParameters params = SinglePhaseFluidProperties::validParams();
  params.addClassDescription(
      "Single phase fluid properties computed using bi-dimensional interpolation of tabulated "
      "values.");
 
  // Which interpolations to create
  params.addParam<bool>("create_pT_interpolations",
                        true,
                        "Whether to load (from file) or create (from a fluid property object) "
                        "properties interpolations from pressure and temperature");
  params.addParam<bool>(
      "create_ve_interpolations",
      false,
      "Whether to load (from file) or create (from a fluid property object) "
      "properties interpolations from specific volume and specific internal energy");
 
  // Input / output
  params.addParam<UserObjectName>("fp", "The name of the FluidProperties UserObject");
  params.deprecateParam("fp", "input_fp", "12/12/26");
  // deprecate to be able to put "fp" in the GlobalParams without creating issues with TabulatedFP
  params.addParam<FileName>("fluid_property_file",
                            "Name of the csv file containing the tabulated fluid property data.");
  params.addParam<FileName>(
      "fluid_property_ve_file",
      "Name of the csv file containing the tabulated (v,e) fluid property data.");
  params.addParam<FileName>("fluid_property_output_file",
                            "Name of the CSV file which can be output with the tabulation. This "
                            "file can then be read as a 'fluid_property_file'");
  params.addParam<FileName>(
      "fluid_property_ve_output_file",
      "Name of the CSV file which can be output with the (v,e) tabulation. This "
      "file can then be read as a 'fluid_property_ve_file'");
  params.addDeprecatedParam<bool>(
      "save_file",
      "Whether to save the csv fluid properties file",
      "This parameter is no longer required. Whether to save a CSV tabulation file is controlled "
      "by specifying the 'fluid_property_output_file' parameter");
  params.addParam<bool>("skip_header_tabulation",
                        false,
                        "Whether to skip the header in the tabulation output, useful for testing");
 
  // Data source on a per-property basis
  MultiMooseEnum properties(
      "density enthalpy internal_energy viscosity k c cv cp entropy pressure temperature",
      "density enthalpy internal_energy viscosity");
  params.addParam<MultiMooseEnum>("interpolated_properties",
                                  properties,
                                  "Properties to interpolate. If unspecified and a data file is "
                                  "provided, the properties from the data file will be used. If "
                                  "specified, some properties from the data file can be ignored.");
 
  // (p,T) grid parameters
  params.addRangeCheckedParam<Real>(
      "temperature_min", 300, "temperature_min > 0", "Minimum temperature for tabulated data.");
  params.addParam<Real>("temperature_max", 500, "Maximum temperature for tabulated data.");
  params.addRangeCheckedParam<Real>(
      "pressure_min", 1e5, "pressure_min > 0", "Minimum pressure for tabulated data.");
  params.addParam<Real>("pressure_max", 50.0e6, "Maximum pressure for tabulated data.");
  params.addRangeCheckedParam<unsigned int>(
      "num_T", 100, "num_T > 0", "Number of points to divide temperature range.");
  params.addRangeCheckedParam<unsigned int>(
      "num_p", 100, "num_p > 0", "Number of points to divide pressure range.");
 
  // (v,e) grid parameters
  params.addParam<Real>("e_min", "Minimum specific internal energy for tabulated data.");
  params.addParam<Real>("e_max", "Maximum specific internal energy for tabulated data.");
  params.addRangeCheckedParam<Real>(
      "v_min", "v_min > 0", "Minimum specific volume for tabulated data.");
  params.addRangeCheckedParam<Real>(
      "v_max", "v_max > 0", "Maximum specific volume for tabulated data.");
  params.addParam<bool>("construct_pT_from_ve",
                        false,
                        "If the lookup table (p, T) as functions of (v, e) should be constructed.");
  params.addParam<bool>("construct_pT_from_vh",
                        false,
                        "If the lookup table (p, T) as functions of (v, h) should be constructed.");
  params.addRangeCheckedParam<unsigned int>(
      "num_v",
      100,
      "num_v > 0",
      "Number of points to divide specific volume range for (v,e) lookups.");
  params.addRangeCheckedParam<unsigned int>("num_e",
                                            100,
                                            "num_e > 0",
                                            "Number of points to divide specific internal energy "
                                            "range for (v,e) lookups.");
  params.addParam<bool>(
      "use_log_grid_v",
      false,
      "Option to use a base-10 logarithmically-spaced grid for specific volume instead of a "
      "linearly-spaced grid.");
  params.addParam<bool>(
      "use_log_grid_e",
      false,
      "Option to use a base-10 logarithmically-spaced grid for specific internal energy instead "
      "of a linearly-spaced grid.");
  params.addParam<bool>(
      "use_log_grid_h",
      false,
      "Option to use a base-10 logarithmically-spaced grid for specific enthalpy instead "
      "of a linearly-spaced grid.");
 
  // Out of bounds behavior
  params.addDeprecatedParam<bool>(
      "error_on_out_of_bounds",
      "Whether pressure or temperature from tabulation exceeding user-specified bounds leads to "
      "an error.",
      "This parameter has been replaced by the 'out_of_bounds_behavior' parameter which offers "
      "more flexibility. The option to error is called 'throw' in that parameter.");
  // NOTE: this enum must remain the same as OOBBehavior in the header
  MooseEnum OOBBehavior("ignore throw declare_invalid warn_invalid set_to_closest_bound", "throw");
  params.addParam<MooseEnum>("out_of_bounds_behavior",
                             OOBBehavior,
                             "Property evaluation behavior when evaluated outside the "
                             "user-specified or tabulation-specified bounds");
 
  // This is generally a bad idea. However, several properties have not been tabulated so several
  // tests are relying on the original fp object to provide the value (for example for the
  // vaporPressure())
  params.addParam<bool>(
      "allow_fp_and_tabulation", false, "Whether to allow the two sources of data concurrently");
 
  params.addParamNamesToGroup("fluid_property_file fluid_property_ve_file "
                              "fluid_property_output_file fluid_property_ve_output_file",
                              "Tabulation file read/write");
  params.addParamNamesToGroup("construct_pT_from_ve construct_pT_from_vh",
                              "Variable set conversion");
  params.addParamNamesToGroup("temperature_min temperature_max pressure_min pressure_max e_min "
                              "e_max v_min v_max error_on_out_of_bounds out_of_bounds_behavior",
                              "Tabulation and interpolation bounds");
  params.addParamNamesToGroup(
      "num_T num_p num_v num_e use_log_grid_v use_log_grid_e use_log_grid_h",
      "Tabulation and interpolation discretization");
 
  return params;
}

Referenced by TabulatedBicubicFluidProperties::validParams().

◆ vaporPressure() [1/3]

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;
}

◆ vaporPressure() [2/3]

Real TabulatedFluidProperties::vaporPressure ( Real T ) const

overridevirtual

Vapor pressure.

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

Parameters

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

Reimplemented from SinglePhaseFluidProperties.

Definition at line 1289 of file TabulatedFluidProperties.C.

{
  if (_fp)
    return _fp->vaporPressure(temperature);
  else
    TabulationNotImplementedError("vaporPressure");
}

◆ vaporPressure() [3/3]

void TabulatedFluidProperties::vaporPressure	(	Real	temperature,
		Real &	psat,
		Real &	dpsat_dT
	)		const

overridevirtual

Reimplemented from SinglePhaseFluidProperties.

Definition at line 1298 of file TabulatedFluidProperties.C.

{
  if (_fp)
    _fp->vaporPressure(temperature, psat, dpsat_dT);
  else
    TabulationNotImplementedError("vaporPressure");
}

◆ vaporTemperature() [1/3]

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;
}

◆ vaporTemperature() [2/3]

Real TabulatedFluidProperties::vaporTemperature ( Real p ) const

overridevirtual

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 from SinglePhaseFluidProperties.

Definition at line 1307 of file TabulatedFluidProperties.C.

{
  if (_fp)
    return _fp->vaporTemperature(pressure);
  else
    TabulationNotImplementedError("vaporTemperature");
}

◆ vaporTemperature() [3/3]

void TabulatedFluidProperties::vaporTemperature	(	Real	pressure,
		Real &	Tsat,
		Real &	dTsat_dp
	)		const

overridevirtual

Reimplemented from SinglePhaseFluidProperties.

Definition at line 1316 of file TabulatedFluidProperties.C.

{
 
  if (_fp)
    _fp->vaporTemperature(pressure, Tsat, dTsat_dp);
  else
    TabulationNotImplementedError("vaporTemperature");
}

◆ writeTabulatedData()

void TabulatedFluidProperties::writeTabulatedData ( std::string file_name )

protected

Writes tabulated data to a file.

Parameters

file_name name of the file to be written

Definition at line 1922 of file TabulatedFluidProperties.C.

{
  if (processor_id() == 0)
  {
    // Write out the (p, T) interpolation tables
    if (_file_name_out != "")
    {
      file_name = file_name.empty() ? "fluid_properties_" + name() + "_out.csv" : file_name;
      MooseUtils::checkFileWriteable(file_name);
 
      std::ofstream file_out(file_name.c_str());
 
      if (!getParam<bool>("skip_header_tabulation"))
      {
        // Write out date and fluid type
        time_t now = std::time(&now);
        file_out << "# " << (_fp ? _fp->fluidName() : "")
                 << " properties (p,T) tabulation created by TabulatedFluidProperties on "
                 << ctime(&now) << "\n";
      }
 
      // Write out column names
      file_out << "pressure, temperature";
      for (std::size_t i = 0; i < _interpolated_properties.size(); ++i)
        if (_interpolated_properties[i] != "pressure" &&
            _interpolated_properties[i] != "temperature")
          file_out << ", " << _interpolated_properties[i];
      file_out << "\n";
 
      // Write out the fluid property data
      for (unsigned int p = 0; p < _num_p; ++p)
        for (unsigned int t = 0; t < _num_T; ++t)
        {
          file_out << _pressure[p] << ", " << _temperature[t];
          for (std::size_t i = 0; i < _properties.size(); ++i)
            file_out << ", " << _properties[i][p * _num_T + t];
          file_out << "\n";
        }
 
      file_out << std::flush;
      file_out.close();
    }
 
    // Write out the (v,e) interpolation tables
    if (_file_name_ve_out != "" && (_construct_pT_from_ve || _create_direct_ve_interpolations))
    {
      const auto file_name_ve = (_file_name_ve_out == "")
                                    ? std::regex_replace(file_name, std::regex("\\.csv"), "_ve.csv")
                                    : _file_name_ve_out;
      MooseUtils::checkFileWriteable(file_name_ve);
      std::ofstream file_out(file_name_ve.c_str());
 
      // Write out date and fluid type
      if (!getParam<bool>("skip_header_tabulation"))
      {
        time_t now = std::time(&now);
        file_out << "# " << (_fp ? _fp->fluidName() : "")
                 << " properties (v,e) tabulation created by TabulatedFluidProperties on "
                 << ctime(&now) << "\n";
      }
 
      // Write out column names
      file_out << "specific_volume, internal_energy, pressure, temperature";
      for (const auto i : index_range(_interpolated_properties))
        // Avoid writing the fixed columns twice
        if (_interpolated_properties[i] != "internal_energy" &&
            _interpolated_properties[i] != "pressure" &&
            _interpolated_properties[i] != "temperature")
          file_out << ", " << _interpolated_properties[i];
      file_out << "\n";
 
      // Write out the fluid property data
      for (const auto v : make_range(_num_v))
        for (const auto e : make_range(_num_e))
        {
          const auto v_val = _specific_volume[v];
          const auto e_val = _internal_energy[e];
          // Use the expected source for the grid. Note that the tabulations are already created
          Real pressure, temperature;
          if (_construct_pT_from_ve)
          {
            pressure = _p_from_v_e_ipol->sample(v_val, e_val);
            temperature = _T_from_v_e_ipol->sample(v_val, e_val);
          }
          else
          {
            pressure = p_from_v_e(v_val, e_val);
            temperature = T_from_v_e(v_val, e_val);
          }
          file_out << v_val << ", " << e_val << ", " << pressure << ", " << temperature
                   << (_interpolated_properties.size() ? ", " : "");
          for (const auto i : index_range(_interpolated_properties))
          {
            bool add_comma = true;
            if (i == _density_idx)
              file_out << 1. / v_val;
            else if (i == _enthalpy_idx)
              file_out << h_from_v_e(v_val, e_val);
            // Note that we could use (p,T) routine to generate this instead of (v,e)
            // Or could use the _properties_ve array similar to what we do for (pressure,
            // temperature)
            else if (i == _viscosity_idx)
              file_out << mu_from_v_e(v_val, e_val);
            else if (i == _k_idx)
              file_out << k_from_v_e(v_val, e_val);
            else if (i == _c_idx)
              file_out << c_from_v_e(v_val, e_val);
            else if (i == _cv_idx)
              file_out << cv_from_v_e(v_val, e_val);
            else if (i == _cp_idx)
              file_out << cp_from_v_e(v_val, e_val);
            else if (i == _entropy_idx)
              file_out << s_from_v_e(v_val, e_val);
            else
              add_comma = false;
            if (i != _interpolated_properties.size() - 1 && add_comma)
              file_out << ", ";
          }
 
          file_out << "\n";
        }
 
      file_out << std::flush;
      file_out.close();
    }
  }
}

Referenced by initialSetup().

◆ 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.

{
  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];
}

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().

Member Data Documentation

◆ _allow_fp_and_tabulation

const bool TabulatedFluidProperties::_allow_fp_and_tabulation

protected

Whether to allow a fp object when a tabulation is in use.

Definition at line 328 of file TabulatedFluidProperties.h.

Referenced by TabulatedFluidProperties().

◆ _allow_imperfect_jacobians

const bool FluidProperties::_allow_imperfect_jacobians

protectedinherited

Flag to set unimplemented Jacobian entries to zero.

Definition at line 47 of file FluidProperties.h.

Referenced by VaporMixtureFluidProperties::imperfectJacobianMessage(), Water97FluidProperties::T_from_p_h_ad(), and SinglePhaseFluidProperties::unimplementedDerivativeMethod().

◆ _c_idx

unsigned int TabulatedFluidProperties::_c_idx

protected

Definition at line 353 of file TabulatedFluidProperties.h.

Referenced by c_from_p_T(), c_from_p_T(), c_from_v_e(), c_from_v_e(), computePropertyIndicesInInterpolationVectors(), and writeTabulatedData().

◆ _construct_pT_from_ve

bool TabulatedFluidProperties::_construct_pT_from_ve

protected

if the lookup table p(v, e) and T(v, e) should be constructed

Definition at line 364 of file TabulatedFluidProperties.h.

Referenced by c_from_v_e(), c_from_v_e(), checkInitialGuess(), TabulatedBicubicFluidProperties::constructInterpolation(), cp_from_v_e(), cp_from_v_e(), cv_from_v_e(), cv_from_v_e(), g_from_v_e(), k_from_v_e(), k_from_v_e(), mu_from_v_e(), mu_from_v_e(), p_from_v_e(), p_from_v_e(), p_from_v_e(), readFileTabulationData(), s_from_v_e(), s_from_v_e(), T_from_v_e(), T_from_v_e(), T_from_v_e(), and writeTabulatedData().

◆ _construct_pT_from_vh

bool TabulatedFluidProperties::_construct_pT_from_vh

protected

if the lookup table p(v, h) and T(v, h) should be constructed

Definition at line 366 of file TabulatedFluidProperties.h.

Referenced by checkInitialGuess(), TabulatedBicubicFluidProperties::constructInterpolation(), e_from_v_h(), and e_from_v_h().

◆ _cp_idx

unsigned int TabulatedFluidProperties::_cp_idx

protected

Definition at line 354 of file TabulatedFluidProperties.h.

Referenced by computePropertyIndicesInInterpolationVectors(), cp_from_p_T(), cp_from_p_T(), cp_from_v_e(), cp_from_v_e(), and writeTabulatedData().

◆ _create_direct_pT_interpolations

const bool TabulatedFluidProperties::_create_direct_pT_interpolations

protected

Whether the object has direct (p,T) interpolations (whether created from file or from _fp)

Definition at line 298 of file TabulatedFluidProperties.h.

Referenced by c_from_p_T(), c_from_p_T(), TabulatedBicubicFluidProperties::constructInterpolation(), cp_from_p_T(), cp_from_p_T(), cv_from_p_T(), e_from_p_T(), e_from_p_T(), e_from_p_T(), g_from_v_e(), h_from_p_T(), h_from_p_T(), h_from_p_T(), initialSetup(), k_from_p_T(), k_from_p_T(), mu_from_p_T(), mu_from_p_T(), rho_from_p_T(), rho_from_p_T(), rho_from_p_T(), rho_from_p_T(), s_from_p_T(), s_from_p_T(), T_from_p_h(), T_from_p_h(), T_from_p_rho(), TabulatedFluidProperties(), v_from_p_T(), v_from_p_T(), and v_from_p_T().

◆ _create_direct_ve_interpolations

const bool TabulatedFluidProperties::_create_direct_ve_interpolations

protected

Whether the object has direct (v,e) interpolations (whether created from file or from _fp)

Definition at line 300 of file TabulatedFluidProperties.h.

Referenced by c_from_v_e(), c_from_v_e(), checkInitialGuess(), TabulatedBicubicFluidProperties::constructInterpolation(), cp_from_v_e(), cp_from_v_e(), cv_from_v_e(), cv_from_v_e(), e_from_p_rho(), e_from_p_rho(), e_from_p_T(), e_from_p_T(), e_from_p_T(), e_from_v_h(), e_from_v_h(), g_from_v_e(), h_from_p_T(), h_from_p_T(), h_from_p_T(), initialSetup(), k_from_v_e(), k_from_v_e(), mu_from_v_e(), mu_from_v_e(), p_from_v_e(), p_from_v_e(), p_from_v_e(), rho_from_p_T(), rho_from_p_T(), rho_from_p_T(), s_from_p_T(), s_from_v_e(), s_from_v_e(), T_from_p_h(), T_from_p_h(), T_from_p_rho(), T_from_p_rho(), T_from_v_e(), T_from_v_e(), T_from_v_e(), TabulatedFluidProperties(), v_from_p_T(), v_from_p_T(), and writeTabulatedData().

◆ _csv_reader

MooseUtils::DelimitedFileReader TabulatedFluidProperties::_csv_reader

protected

The MOOSE delimited file reader.

Definition at line 361 of file TabulatedFluidProperties.h.

Referenced by readFileTabulationData(), and TabulatedFluidProperties().

◆ _cv_idx

unsigned int TabulatedFluidProperties::_cv_idx

protected

Definition at line 355 of file TabulatedFluidProperties.h.

Referenced by computePropertyIndicesInInterpolationVectors(), cv_from_p_T(), cv_from_p_T(), cv_from_v_e(), cv_from_v_e(), and writeTabulatedData().

◆ _density_idx

unsigned int TabulatedFluidProperties::_density_idx

protected

Index of each property.

Definition at line 348 of file TabulatedFluidProperties.h.

Referenced by computePropertyIndicesInInterpolationVectors(), createVGridVector(), rho_from_p_T(), rho_from_p_T(), rho_from_p_T(), rho_from_p_T(), v_from_p_T(), v_from_p_T(), v_from_p_T(), and writeTabulatedData().

◆ _e_bounds_specified

bool TabulatedFluidProperties::_e_bounds_specified

protected

Whether the specific internal energy bounds were set by the user.

Definition at line 405 of file TabulatedFluidProperties.h.

Referenced by createVEGridVectors(), readFileTabulationData(), and TabulatedFluidProperties().

◆ _e_max

Real TabulatedFluidProperties::_e_max

protected

Maximum internal energy in tabulated data (can be user-specified)

Definition at line 411 of file TabulatedFluidProperties.h.

Referenced by checkInputVariablesVE(), createVEGridVectors(), e_from_p_rho(), e_from_p_rho(), e_from_p_T(), e_from_p_T(), readFileTabulationData(), TabulatedFluidProperties(), v_from_p_T(), and v_from_p_T().

◆ _e_min

Real TabulatedFluidProperties::_e_min

protected

Minimum internal energy in tabulated data (can be user-specified)

Definition at line 409 of file TabulatedFluidProperties.h.

Referenced by checkInputVariablesVE(), createVEGridVectors(), e_from_p_rho(), e_from_p_rho(), e_from_p_T(), e_from_p_T(), readFileTabulationData(), TabulatedFluidProperties(), v_from_p_T(), and v_from_p_T().

◆ _enthalpy

std::vector<Real> TabulatedFluidProperties::_enthalpy

protected

Specific enthalpy vector.

Definition at line 295 of file TabulatedFluidProperties.h.

Referenced by TabulatedBicubicFluidProperties::constructInterpolation(), and createVHGridVectors().

◆ _enthalpy_idx

unsigned int TabulatedFluidProperties::_enthalpy_idx

protected

Definition at line 349 of file TabulatedFluidProperties.h.

Referenced by computePropertyIndicesInInterpolationVectors(), createVHGridVectors(), g_from_v_e(), h_from_p_T(), h_from_p_T(), h_from_p_T(), and writeTabulatedData().

◆ _entropy_idx

unsigned int TabulatedFluidProperties::_entropy_idx

protected

Definition at line 356 of file TabulatedFluidProperties.h.

Referenced by computePropertyIndicesInInterpolationVectors(), g_from_v_e(), s_from_p_T(), s_from_p_T(), s_from_v_e(), s_from_v_e(), and writeTabulatedData().

◆ _file_name_in

FileName TabulatedFluidProperties::_file_name_in

protected

File name of input tabulated data file.

Definition at line 276 of file TabulatedFluidProperties.h.

Referenced by checkInitialGuess(), initialSetup(), readFileTabulationData(), and TabulatedFluidProperties().

◆ _file_name_out

FileName TabulatedFluidProperties::_file_name_out

protected

File name of output tabulated data file.

Definition at line 280 of file TabulatedFluidProperties.h.

Referenced by initialSetup(), and writeTabulatedData().

◆ _file_name_ve_in

FileName TabulatedFluidProperties::_file_name_ve_in

protected

File name of input (v,e) tabulated data file.

Definition at line 278 of file TabulatedFluidProperties.h.

Referenced by checkInitialGuess(), createVGridVector(), createVHGridVectors(), initialSetup(), readFileTabulationData(), and TabulatedFluidProperties().

◆ _file_name_ve_out

FileName TabulatedFluidProperties::_file_name_ve_out

protected

File name of output (v,e) tabulated data file.

Definition at line 282 of file TabulatedFluidProperties.h.

Referenced by writeTabulatedData().

◆ _fp

const SinglePhaseFluidProperties* const TabulatedFluidProperties::_fp

protected

SinglePhaseFluidPropertiesPT UserObject.

Definition at line 326 of file TabulatedFluidProperties.h.

Referenced by c_from_p_T(), c_from_p_T(), c_from_v_e(), c_from_v_e(), checkInitialGuess(), TabulatedBicubicFluidProperties::constructInterpolation(), cp_from_p_T(), cp_from_p_T(), cp_from_v_e(), cp_from_v_e(), createVEGridVectors(), createVGridVector(), createVHGridVectors(), criticalDensity(), criticalPressure(), criticalTemperature(), cv_from_p_T(), cv_from_p_T(), cv_from_v_e(), cv_from_v_e(), e_from_p_T(), e_from_p_T(), e_from_p_T(), e_from_v_h(), e_from_v_h(), fluidName(), g_from_v_e(), generateTabulatedData(), generateVETabulatedData(), h_from_p_T(), h_from_p_T(), h_from_p_T(), henryCoefficients(), initialSetup(), k_from_p_T(), k_from_p_T(), k_from_v_e(), k_from_v_e(), molarMass(), mu_from_p_T(), mu_from_p_T(), mu_from_v_e(), mu_from_v_e(), TabulatedBicubicFluidProperties::outputWarnings(), p_from_v_e(), p_from_v_e(), p_from_v_e(), rho_from_p_T(), rho_from_p_T(), rho_from_p_T(), rho_from_p_T(), s_from_h_p(), s_from_p_T(), s_from_p_T(), s_from_v_e(), s_from_v_e(), T_from_p_h(), T_from_p_h(), T_from_v_e(), T_from_v_e(), T_from_v_e(), TabulatedFluidProperties(), triplePointPressure(), triplePointTemperature(), v_from_p_T(), v_from_p_T(), v_from_p_T(), vaporPressure(), vaporPressure(), vaporTemperature(), vaporTemperature(), and writeTabulatedData().

◆ _h_max

Real TabulatedFluidProperties::_h_max

protected

Maximum specific enthalpy in tabulated data.

Definition at line 419 of file TabulatedFluidProperties.h.

Referenced by createVHGridVectors().

◆ _h_min

Real TabulatedFluidProperties::_h_min

protected

Minimum specific enthalpy in tabulated data.

Definition at line 417 of file TabulatedFluidProperties.h.

Referenced by createVHGridVectors().

◆ _initial_setup_done

bool TabulatedFluidProperties::_initial_setup_done

protected

keeps track of whether initialSetup has been performed

Definition at line 368 of file TabulatedFluidProperties.h.

Referenced by initialSetup().

◆ _internal_energy

std::vector<Real> TabulatedFluidProperties::_internal_energy

protected

Specific internal energy vector.

Definition at line 293 of file TabulatedFluidProperties.h.

Referenced by TabulatedBicubicFluidProperties::constructInterpolation(), createVEGridVectors(), generateVETabulatedData(), readFileTabulationData(), and writeTabulatedData().

◆ _internal_energy_idx

unsigned int TabulatedFluidProperties::_internal_energy_idx

protected

Definition at line 350 of file TabulatedFluidProperties.h.

Referenced by computePropertyIndicesInInterpolationVectors(), createVEGridVectors(), e_from_p_T(), e_from_p_T(), and e_from_p_T().

◆ _interpolate_c

bool TabulatedFluidProperties::_interpolate_c

protected

Definition at line 340 of file TabulatedFluidProperties.h.

Referenced by c_from_p_T(), c_from_p_T(), c_from_v_e(), c_from_v_e(), and computePropertyIndicesInInterpolationVectors().

◆ _interpolate_cp

bool TabulatedFluidProperties::_interpolate_cp

protected

Definition at line 341 of file TabulatedFluidProperties.h.

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

◆ _interpolate_cv

bool TabulatedFluidProperties::_interpolate_cv

protected

Definition at line 342 of file TabulatedFluidProperties.h.

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

◆ _interpolate_density

bool TabulatedFluidProperties::_interpolate_density

protected

Set of flags to note whether a property is to be interpolated.

Definition at line 335 of file TabulatedFluidProperties.h.

Referenced by computePropertyIndicesInInterpolationVectors(), createVGridVector(), rho_from_p_T(), rho_from_p_T(), rho_from_p_T(), rho_from_p_T(), T_from_p_rho(), T_from_p_rho(), v_from_p_T(), v_from_p_T(), and v_from_p_T().

◆ _interpolate_enthalpy

bool TabulatedFluidProperties::_interpolate_enthalpy

protected

Definition at line 336 of file TabulatedFluidProperties.h.

Referenced by computePropertyIndicesInInterpolationVectors(), h_from_p_T(), h_from_p_T(), and h_from_p_T().

◆ _interpolate_entropy

bool TabulatedFluidProperties::_interpolate_entropy

protected

Definition at line 343 of file TabulatedFluidProperties.h.

Referenced by computePropertyIndicesInInterpolationVectors(), s_from_p_T(), s_from_p_T(), s_from_v_e(), and s_from_v_e().

◆ _interpolate_internal_energy

bool TabulatedFluidProperties::_interpolate_internal_energy

protected

Definition at line 337 of file TabulatedFluidProperties.h.

Referenced by computePropertyIndicesInInterpolationVectors(), createVEGridVectors(), e_from_p_T(), e_from_p_T(), and e_from_p_T().

◆ _interpolate_k

bool TabulatedFluidProperties::_interpolate_k

protected

Definition at line 339 of file TabulatedFluidProperties.h.

Referenced by computePropertyIndicesInInterpolationVectors(), k_from_p_T(), k_from_p_T(), k_from_v_e(), and k_from_v_e().

◆ _interpolate_pressure

bool TabulatedFluidProperties::_interpolate_pressure

protected

Definition at line 344 of file TabulatedFluidProperties.h.

Referenced by computePropertyIndicesInInterpolationVectors(), p_from_v_e(), p_from_v_e(), and p_from_v_e().

◆ _interpolate_temperature

bool TabulatedFluidProperties::_interpolate_temperature

protected

Definition at line 345 of file TabulatedFluidProperties.h.

Referenced by computePropertyIndicesInInterpolationVectors(), T_from_v_e(), T_from_v_e(), and T_from_v_e().

◆ _interpolate_viscosity

bool TabulatedFluidProperties::_interpolate_viscosity

protected

Definition at line 338 of file TabulatedFluidProperties.h.

Referenced by computePropertyIndicesInInterpolationVectors(), mu_from_p_T(), mu_from_p_T(), mu_from_v_e(), and mu_from_v_e().

◆ _interpolated_properties

std::vector<std::string> TabulatedFluidProperties::_interpolated_properties

protected

List of properties to be interpolated.

Definition at line 333 of file TabulatedFluidProperties.h.

Referenced by computePropertyIndicesInInterpolationVectors(), generateTabulatedData(), generateVETabulatedData(), readFileTabulationData(), and writeTabulatedData().

◆ _interpolated_properties_enum

MultiMooseEnum TabulatedFluidProperties::_interpolated_properties_enum

protected

Properties to be interpolated entered in the input file.

Definition at line 331 of file TabulatedFluidProperties.h.

Referenced by generateTabulatedData(), generateVETabulatedData(), and readFileTabulationData().

◆ _k_idx

unsigned int TabulatedFluidProperties::_k_idx

protected

Definition at line 352 of file TabulatedFluidProperties.h.

Referenced by computePropertyIndicesInInterpolationVectors(), k_from_p_T(), k_from_p_T(), k_from_v_e(), k_from_v_e(), and writeTabulatedData().

◆ _log_space_e

bool TabulatedFluidProperties::_log_space_e

protected

log-space the internal energy interpolation grid axis instead of linear

Definition at line 376 of file TabulatedFluidProperties.h.

Referenced by createVEGridVectors(), and TabulatedFluidProperties().

◆ _log_space_h

bool TabulatedFluidProperties::_log_space_h

protected

log-space the enthalpy interpolation grid axis instead of linear

Definition at line 378 of file TabulatedFluidProperties.h.

Referenced by createVHGridVectors().

◆ _log_space_v

bool TabulatedFluidProperties::_log_space_v

protected

log-space the specific volume interpolation grid axis instead of linear

Definition at line 374 of file TabulatedFluidProperties.h.

Referenced by createVGridVector(), and TabulatedFluidProperties().

◆ _max_newton_its

const unsigned int SinglePhaseFluidProperties::_max_newton_its

protectedinherited

Maximum number of iterations for the variable conversion newton solves.

Definition at line 449 of file SinglePhaseFluidProperties.h.

Referenced by e_from_p_rho(), e_from_p_rho(), e_from_p_T(), e_from_p_T(), e_from_v_h(), e_from_v_h(), SinglePhaseFluidProperties::p_T_from_h_s(), SinglePhaseFluidProperties::p_T_from_v_e(), SinglePhaseFluidProperties::p_T_from_v_h(), SodiumSaturationFluidProperties::rho_from_p_s(), SodiumSaturationFluidProperties::rho_from_p_s(), T_from_p_h(), SimpleFluidProperties::T_from_p_h(), SodiumSaturationFluidProperties::T_from_p_h(), TemperaturePressureFunctionFluidProperties::T_from_p_h(), T_from_p_h(), T_from_p_rho(), NaKFluidProperties::T_from_p_rho(), T_from_p_rho(), T_from_p_s(), v_from_p_T(), and v_from_p_T().

◆ _num_e

unsigned int TabulatedFluidProperties::_num_e

protected

Number of internal energy points in tabulated data.

Definition at line 372 of file TabulatedFluidProperties.h.

Referenced by TabulatedBicubicFluidProperties::constructInterpolation(), createVEGridVectors(), createVHGridVectors(), generateVETabulatedData(), readFileTabulationData(), and writeTabulatedData().

◆ _num_p

unsigned int TabulatedFluidProperties::_num_p

protected

Number of pressure points in the tabulated data.

Definition at line 323 of file TabulatedFluidProperties.h.

Referenced by TabulatedBicubicFluidProperties::constructInterpolation(), generateTabulatedData(), readFileTabulationData(), and writeTabulatedData().

◆ _num_T

unsigned int TabulatedFluidProperties::_num_T

protected

Number of temperature points in the tabulated data.

Definition at line 321 of file TabulatedFluidProperties.h.

Referenced by TabulatedBicubicFluidProperties::constructInterpolation(), generateTabulatedData(), readFileTabulationData(), and writeTabulatedData().

◆ _num_v

unsigned int TabulatedFluidProperties::_num_v

protected

Number of specific volume points in the tabulated data.

Definition at line 370 of file TabulatedFluidProperties.h.

Referenced by TabulatedBicubicFluidProperties::constructInterpolation(), createVGridVector(), generateVETabulatedData(), readFileTabulationData(), and writeTabulatedData().

◆ _OOBBehavior

MooseEnum TabulatedFluidProperties::_OOBBehavior

protected

User-selected out-of-bounds behavior.

Definition at line 381 of file TabulatedFluidProperties.h.

Referenced by checkInputVariables(), checkInputVariablesVE(), TabulatedBicubicFluidProperties::constructInterpolation(), and TabulatedFluidProperties().

◆ _p_from_v_e_ipol

std::unique_ptr<BidimensionalInterpolation> TabulatedFluidProperties::_p_from_v_e_ipol

protected

Bi-dimensional interpolation of pressure from (v,e)

Definition at line 396 of file TabulatedFluidProperties.h.

Referenced by c_from_v_e(), c_from_v_e(), TabulatedBicubicFluidProperties::constructInterpolation(), cp_from_v_e(), cp_from_v_e(), cv_from_v_e(), cv_from_v_e(), k_from_v_e(), k_from_v_e(), mu_from_v_e(), mu_from_v_e(), p_from_v_e(), p_from_v_e(), p_from_v_e(), s_from_v_e(), s_from_v_e(), and writeTabulatedData().

◆ _p_from_v_h_ipol

std::unique_ptr<BidimensionalInterpolation> TabulatedFluidProperties::_p_from_v_h_ipol

protected

Bidimensional interpolation of pressure from (v,h)

Definition at line 402 of file TabulatedFluidProperties.h.

Referenced by TabulatedBicubicFluidProperties::constructInterpolation(), e_from_v_h(), and e_from_v_h().

◆ _p_idx

unsigned int TabulatedFluidProperties::_p_idx

protected

Definition at line 357 of file TabulatedFluidProperties.h.

Referenced by computePropertyIndicesInInterpolationVectors(), p_from_v_e(), p_from_v_e(), and p_from_v_e().

◆ _p_initial_guess

const Real SinglePhaseFluidProperties::_p_initial_guess

protectedinherited

Initial guess for pressure (or pressure used to compute the initial guess)

Definition at line 447 of file SinglePhaseFluidProperties.h.

Referenced by checkInitialGuess(), TabulatedBicubicFluidProperties::constructInterpolation(), TemperaturePressureFunctionFluidProperties::cp_from_v_e(), TemperaturePressureFunctionFluidProperties::cv_from_v_e(), TemperaturePressureFunctionFluidProperties::cv_from_v_e(), e_from_v_h(), e_from_v_h(), g_from_v_e(), TemperaturePressureFunctionFluidProperties::k_from_v_e(), TemperaturePressureFunctionFluidProperties::mu_from_v_e(), TemperaturePressureFunctionFluidProperties::p_from_v_e(), Water97FluidProperties::p_from_v_e_template(), Water97FluidProperties::p_T_from_v_h(), T_from_h_s(), and TemperaturePressureFunctionFluidProperties::T_from_v_e().

◆ _pressure

std::vector<Real> TabulatedFluidProperties::_pressure

protected

Pressure vector.

Definition at line 287 of file TabulatedFluidProperties.h.

Referenced by TabulatedBicubicFluidProperties::constructInterpolation(), generateTabulatedData(), readFileTabulationData(), and writeTabulatedData().

◆ _pressure_max

Real TabulatedFluidProperties::_pressure_max

protected

Maximum pressure in tabulated data.

Definition at line 319 of file TabulatedFluidProperties.h.

Referenced by checkInitialGuess(), checkInputVariables(), TabulatedBicubicFluidProperties::constructInterpolation(), createVEGridVectors(), createVGridVector(), createVHGridVectors(), generateTabulatedData(), TabulatedBicubicFluidProperties::outputWarnings(), readFileTabulationData(), and TabulatedFluidProperties().

◆ _pressure_min

Real TabulatedFluidProperties::_pressure_min

protected

Minimum pressure in tabulated data.

Definition at line 317 of file TabulatedFluidProperties.h.

Referenced by checkInitialGuess(), checkInputVariables(), TabulatedBicubicFluidProperties::constructInterpolation(), createVEGridVectors(), createVGridVector(), createVHGridVectors(), generateTabulatedData(), TabulatedBicubicFluidProperties::outputWarnings(), readFileTabulationData(), and TabulatedFluidProperties().

◆ _properties

std::vector<std::vector<Real> > TabulatedFluidProperties::_properties

protected

Tabulated fluid properties (read from file OR computed from _fp)

Definition at line 303 of file TabulatedFluidProperties.h.

Referenced by TabulatedBicubicFluidProperties::constructInterpolation(), createVEGridVectors(), createVGridVector(), createVHGridVectors(), generateTabulatedData(), readFileTabulationData(), and writeTabulatedData().

◆ _properties_ve

std::vector<std::vector<Real> > TabulatedFluidProperties::_properties_ve

protected

Tabulated fluid properties in (v,e) (read from file OR computed from _fp)

Definition at line 305 of file TabulatedFluidProperties.h.

Referenced by TabulatedBicubicFluidProperties::constructInterpolation(), createVHGridVectors(), generateVETabulatedData(), and readFileTabulationData().

◆ _property_ipol

std::vector<std::unique_ptr<BidimensionalInterpolation> > TabulatedFluidProperties::_property_ipol

protected

Vector of bi-dimensional interpolation of fluid properties.

Definition at line 308 of file TabulatedFluidProperties.h.

Referenced by c_from_p_T(), c_from_p_T(), TabulatedBicubicFluidProperties::constructInterpolation(), cp_from_p_T(), cp_from_p_T(), cv_from_p_T(), cv_from_p_T(), e_from_p_T(), e_from_p_T(), e_from_p_T(), h_from_p_T(), h_from_p_T(), h_from_p_T(), k_from_p_T(), k_from_p_T(), mu_from_p_T(), mu_from_p_T(), rho_from_p_T(), rho_from_p_T(), rho_from_p_T(), rho_from_p_T(), s_from_p_T(), s_from_p_T(), v_from_p_T(), v_from_p_T(), and v_from_p_T().

◆ _property_ve_ipol

std::vector<std::unique_ptr<BidimensionalInterpolation> > TabulatedFluidProperties::_property_ve_ipol

protected

Vector of bi-dimensional interpolation of fluid properties directly in (v,e)

Definition at line 310 of file TabulatedFluidProperties.h.

Referenced by c_from_v_e(), c_from_v_e(), TabulatedBicubicFluidProperties::constructInterpolation(), cp_from_v_e(), cp_from_v_e(), cv_from_v_e(), cv_from_v_e(), g_from_v_e(), h_from_p_T(), h_from_p_T(), h_from_p_T(), k_from_v_e(), k_from_v_e(), mu_from_v_e(), mu_from_v_e(), p_from_v_e(), p_from_v_e(), p_from_v_e(), s_from_p_T(), s_from_v_e(), s_from_v_e(), T_from_v_e(), T_from_v_e(), and T_from_v_e().

◆ _R

const Real FluidProperties::_R = 8.3144598

staticinherited

Universal gas constant (J/mol/K)

Definition at line 41 of file FluidProperties.h.

◆ _save_file

const bool TabulatedFluidProperties::_save_file

protected

Whether to save a generated fluid properties file to disk.

Definition at line 284 of file TabulatedFluidProperties.h.

Referenced by initialSetup().

◆ _specific_volume

std::vector<Real> TabulatedFluidProperties::_specific_volume

protected

Specific volume vector.

Definition at line 291 of file TabulatedFluidProperties.h.

Referenced by TabulatedBicubicFluidProperties::checkNaNs(), TabulatedBicubicFluidProperties::constructInterpolation(), createVGridVector(), generateVETabulatedData(), readFileTabulationData(), and writeTabulatedData().

◆ _T_c2k

const Real FluidProperties::_T_c2k

protectedinherited

Conversion of temperature from Celsius to Kelvin.

Definition at line 45 of file FluidProperties.h.

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

◆ _T_from_v_e_ipol

std::unique_ptr<BidimensionalInterpolation> TabulatedFluidProperties::_T_from_v_e_ipol

protected

Bi-dimensional interpolation of temperature from (v,e)

Definition at line 393 of file TabulatedFluidProperties.h.

Referenced by c_from_v_e(), c_from_v_e(), TabulatedBicubicFluidProperties::constructInterpolation(), cp_from_v_e(), cp_from_v_e(), cv_from_v_e(), cv_from_v_e(), k_from_v_e(), k_from_v_e(), mu_from_v_e(), mu_from_v_e(), s_from_v_e(), s_from_v_e(), T_from_v_e(), T_from_v_e(), T_from_v_e(), and writeTabulatedData().

◆ _T_from_v_h_ipol

std::unique_ptr<BidimensionalInterpolation> TabulatedFluidProperties::_T_from_v_h_ipol

protected

Bi-dimensional interpolation of temperature from (v,h)

Definition at line 399 of file TabulatedFluidProperties.h.

Referenced by TabulatedBicubicFluidProperties::constructInterpolation(), e_from_v_h(), and e_from_v_h().

◆ _T_idx

unsigned int TabulatedFluidProperties::_T_idx

protected

Definition at line 358 of file TabulatedFluidProperties.h.

Referenced by computePropertyIndicesInInterpolationVectors(), g_from_v_e(), T_from_v_e(), T_from_v_e(), and T_from_v_e().

◆ _T_initial_guess

const Real SinglePhaseFluidProperties::_T_initial_guess

protectedinherited

Initial guess for temperature (or temperature used to compute the initial guess)

Definition at line 445 of file SinglePhaseFluidProperties.h.

◆ _temperature

std::vector<Real> TabulatedFluidProperties::_temperature

protected

Temperature vector.

Definition at line 289 of file TabulatedFluidProperties.h.

Referenced by TabulatedBicubicFluidProperties::constructInterpolation(), generateTabulatedData(), readFileTabulationData(), and writeTabulatedData().

◆ _temperature_max

Real TabulatedFluidProperties::_temperature_max

protected

Maximum temperature in tabulated data.

Definition at line 315 of file TabulatedFluidProperties.h.

Referenced by checkInitialGuess(), checkInputVariables(), TabulatedBicubicFluidProperties::constructInterpolation(), createVEGridVectors(), createVGridVector(), createVHGridVectors(), generateTabulatedData(), TabulatedBicubicFluidProperties::outputWarnings(), readFileTabulationData(), and TabulatedFluidProperties().

◆ _temperature_min

Real TabulatedFluidProperties::_temperature_min

protected

Minimum temperature in tabulated data.

Definition at line 313 of file TabulatedFluidProperties.h.

Referenced by checkInitialGuess(), checkInputVariables(), TabulatedBicubicFluidProperties::constructInterpolation(), createVEGridVectors(), createVGridVector(), createVHGridVectors(), generateTabulatedData(), TabulatedBicubicFluidProperties::outputWarnings(), readFileTabulationData(), and TabulatedFluidProperties().

◆ _tolerance

const Real SinglePhaseFluidProperties::_tolerance

protectedinherited

Newton's method may be used to convert between variable sets.

Relative tolerance of the solves

Definition at line 443 of file SinglePhaseFluidProperties.h.

Referenced by e_from_p_rho(), e_from_p_rho(), e_from_p_T(), e_from_p_T(), e_from_v_h(), e_from_v_h(), TemperaturePressureFunctionFluidProperties::p_from_v_e(), Water97FluidProperties::p_from_v_e_template(), SinglePhaseFluidProperties::p_T_from_h_s(), SinglePhaseFluidProperties::p_T_from_v_e(), SinglePhaseFluidProperties::p_T_from_v_h(), SodiumSaturationFluidProperties::rho_from_p_s(), SodiumSaturationFluidProperties::rho_from_p_s(), Water97FluidProperties::T_drhodT_from_p_rho(), T_from_p_h(), SimpleFluidProperties::T_from_p_h(), SodiumSaturationFluidProperties::T_from_p_h(), TemperaturePressureFunctionFluidProperties::T_from_p_h(), HelmholtzFluidProperties::T_from_p_h(), T_from_p_h(), T_from_p_rho(), TemperaturePressureFunctionFluidProperties::T_from_p_rho(), NaKFluidProperties::T_from_p_rho(), T_from_p_rho(), T_from_p_s(), v_from_p_T(), and v_from_p_T().

◆ _v_bounds_specified

bool TabulatedFluidProperties::_v_bounds_specified

protected

Whether the specific volume bounds were set by the user.

Definition at line 407 of file TabulatedFluidProperties.h.

Referenced by createVGridVector(), readFileTabulationData(), and TabulatedFluidProperties().

◆ _v_max

Real TabulatedFluidProperties::_v_max

protected

Maximum specific volume in tabulated data (can be user-specified)

Definition at line 415 of file TabulatedFluidProperties.h.

Referenced by checkInputVariablesVE(), TabulatedBicubicFluidProperties::checkNaNs(), createVGridVector(), readFileTabulationData(), TabulatedFluidProperties(), v_from_p_T(), and v_from_p_T().

◆ _v_min

Real TabulatedFluidProperties::_v_min

protected

Minimum specific volume in tabulated data (can be user-specified)

Definition at line 413 of file TabulatedFluidProperties.h.

Referenced by checkInputVariablesVE(), TabulatedBicubicFluidProperties::checkNaNs(), createVGridVector(), readFileTabulationData(), TabulatedFluidProperties(), v_from_p_T(), and v_from_p_T().

◆ _verbose_newton

const bool SinglePhaseFluidProperties::_verbose_newton

protectedinherited

Whether to output information about newton solves to console.

Definition at line 451 of file SinglePhaseFluidProperties.h.

Referenced by e_from_p_rho(), e_from_p_rho(), e_from_p_T(), e_from_p_T(), e_from_v_h(), e_from_v_h(), SinglePhaseFluidProperties::p_T_from_h_s(), SinglePhaseFluidProperties::p_T_from_v_e(), SinglePhaseFluidProperties::p_T_from_v_h(), SodiumSaturationFluidProperties::rho_from_p_s(), SodiumSaturationFluidProperties::rho_from_p_s(), T_from_p_h(), SodiumSaturationFluidProperties::T_from_p_h(), T_from_p_h(), T_from_p_rho(), T_from_p_rho(), T_from_p_s(), v_from_p_T(), and v_from_p_T().

◆ _viscosity_idx

unsigned int TabulatedFluidProperties::_viscosity_idx

protected

Definition at line 351 of file TabulatedFluidProperties.h.

Referenced by computePropertyIndicesInInterpolationVectors(), mu_from_p_T(), mu_from_p_T(), mu_from_v_e(), mu_from_v_e(), and writeTabulatedData().

◆ h

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

inherited

Definition at line 212 of file SinglePhaseFluidProperties.h.

◆ p [1/10]

e e e e SinglePhaseFluidProperties::p

inherited

Definition at line 190 of file SinglePhaseFluidProperties.h.

◆ p [2/10]

e e e e s SinglePhaseFluidProperties::p

inherited

Definition at line 192 of file SinglePhaseFluidProperties.h.

◆ p [3/10]

e e e e s T T SinglePhaseFluidProperties::p

inherited

Definition at line 196 of file SinglePhaseFluidProperties.h.

◆ p [4/10]

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

inherited

Definition at line 198 of file SinglePhaseFluidProperties.h.

◆ p [5/10]

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

inherited

Definition at line 200 of file SinglePhaseFluidProperties.h.

◆ p [6/10]

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

inherited

Definition at line 202 of file SinglePhaseFluidProperties.h.

◆ p [7/10]

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

inherited

Definition at line 208 of file SinglePhaseFluidProperties.h.

◆ p [8/10]

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

inherited

Definition at line 214 of file SinglePhaseFluidProperties.h.

◆ p [9/10]

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

inherited

Definition at line 216 of file SinglePhaseFluidProperties.h.

◆ p [10/10]

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

inherited

Definition at line 218 of file SinglePhaseFluidProperties.h.

◆ rho

e e e e s T SinglePhaseFluidProperties::rho

inherited

Definition at line 194 of file SinglePhaseFluidProperties.h.

◆ T [1/2]

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

inherited

Definition at line 204 of file SinglePhaseFluidProperties.h.

◆ T [2/2]

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

inherited

Definition at line 206 of file SinglePhaseFluidProperties.h.

◆ v [1/5]

SinglePhaseFluidProperties::v

inherited

Definition at line 182 of file SinglePhaseFluidProperties.h.

◆ v [2/5]

e SinglePhaseFluidProperties::v

inherited

Definition at line 184 of file SinglePhaseFluidProperties.h.

◆ v [3/5]

e e SinglePhaseFluidProperties::v

inherited

Definition at line 186 of file SinglePhaseFluidProperties.h.

◆ v [4/5]

e e e SinglePhaseFluidProperties::v

inherited

Definition at line 188 of file SinglePhaseFluidProperties.h.

◆ v [5/5]

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

inherited

Definition at line 210 of file SinglePhaseFluidProperties.h.

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

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

Public Types

Public Member Functions

Static Public Member Functions

Public Attributes

Static Public Attributes

Protected Types

Protected Member Functions

Static Protected Member Functions

Protected Attributes

Static Protected Attributes

Private Member Functions

Static Private Member Functions

Private Attributes

Detailed Description

Member Enumeration Documentation

◆ OOBBehavior

Constructor & Destructor Documentation

◆ TabulatedFluidProperties()

Member Function Documentation

◆ c_from_p_T() [1/2]

◆ c_from_p_T() [2/2]

◆ c_from_v_e() [1/2]

◆ c_from_v_e() [2/2]

◆ checkFileTabulationGrids()

◆ checkInitialGuess()

◆ checkInputVariables()

◆ checkInputVariablesVE()

◆ computePropertyIndicesInInterpolationVectors()

◆ constructInterpolation()

◆ cp_from_p_T() [1/2]

◆ cp_from_p_T() [2/2]

◆ cp_from_v_e() [1/2]

◆ cp_from_v_e() [2/2]

◆ createVEGridVectors()

◆ createVGridVector()

◆ createVHGridVectors()

◆ criticalDensity()

◆ criticalInternalEnergy()

◆ criticalPressure()

◆ criticalTemperature()

◆ cv_from_p_T() [1/2]

◆ cv_from_p_T() [2/2]

◆ cv_from_v_e() [1/2]

◆ cv_from_v_e() [2/2]

◆ e_from_p_rho() [1/3]

◆ e_from_p_rho() [2/3]

◆ e_from_p_rho() [3/3]

◆ e_from_p_T() [1/3]

◆ e_from_p_T() [2/3]

◆ e_from_p_T() [3/3]

◆ e_from_v_h() [1/2]

◆ e_from_v_h() [2/2]

◆ e_spndl_from_v()

◆ execute()

◆ finalize()

◆ fluidName()

◆ g_from_v_e()

◆ generateTabulatedData()

◆ generateVETabulatedData()

◆ h_from_p_T() [1/3]

◆ h_from_p_T() [2/3]

◆ h_from_p_T() [3/3]

◆ henryCoefficients()

◆ initialize()

◆ initialSetup()

◆ k_from_p_T() [1/2]

◆ k_from_p_T() [2/2]

◆ k_from_v_e() [1/2]

◆ k_from_v_e() [2/2]

◆ makeZeroAndOne() [1/2]

◆ makeZeroAndOne() [2/2]

◆ missingVEInterpolationError()

◆ molarMass()

◆ mu_from_p_T() [1/2]

◆ mu_from_p_T() [2/2]

◆ mu_from_v_e() [1/2]

◆ mu_from_v_e() [2/2]

◆ NeedTabulationError()

◆ NeedTabulationOrFPError()

◆ p_from_v_e() [1/3]