C_N_VectorContent_Gmm | |
CActiveInitializer | |
►CBaseActive | |
CGenericActive< double > | |
CGenericActive< valuetype > | |
►Cstd::basic_string< Char > | STL class |
►Cstd::string | STL class |
Cfstring | Utility class with variable format |
►CCalculatable | Abstract mixin with the interface that has to be implemented by a Model capable of being solved both in simultaneous and in sequential mode |
►CEdgeBase | |
►CStream | Edge model for the mass and energy balance of a generic stream semi-abstract class Contains P, T and one Phase subobject: total phase |
►CStreamTwo< FlashVl > | |
CStreamTabularLiquidLiquid | |
CStreamTabularLiquidVapor | |
►CStreamBaseSimple | |
CStreamSimple< NV, NL, NS > | |
CStreamIapwsLiquidVapor | |
CStreamOne | Stream with a single fluid phase |
CStreamOneSolid | Parameterized stream with a single fluid phase and one solid phase |
CStreamTwo< F > | Stream with two fluid phases, use for VL or LL equilibria |
CStreamTwoSolid< F > | Stream with two fluid phases and one solid use for vapor-liquid solid or liquid-liquid-solid streams |
►CVertexBase | Base of the hierarchy of all vertex model types to be included in a FlowSheet This class manages the connection of vertexes with edges and derived classes must implement the Calculatable interface |
►CConnectivity | Vertex connectivity |
CCompressor | |
CDegasser | |
CDivider | Vertex model to represent a multi-stream Divider (i.e. a tee or multi-way valve) |
CExchanger | |
CFlashDegasser | Parameterized vertex model to represent an (optionally reactive) flash drum with many inlets and two outlets: one vapor phase outlet stream and one liquid / condensate / solid phase outlet stream |
►CFlashDrum | |
CEjector | |
CHeatTransfer | |
CPipe | Model for a pipe object for liquids |
CPump | Simple class for liquid pump calculation |
CFlashSplitter | Parameterized vertex model to represent an (optionally reactive) Flash drum with many inlets and X outlets |
►CFlowSheet | |
CColumn | |
CCompressionStage | |
CDecanter | |
CFallingFilm | |
CLiquidRingVacuumPump | Liquid ring vacuum pump model
Port list: |
►CMultiStage | Vertex model to represent a generic multi-stage countercurrent unit |
CColumnSection | |
CMultiStage2D | Vertex model to represent a generic 2D distributed unit Vertex numbering from 0 to nX-1, from 0 to nY - 1 |
►CMultiStageOneTwo | Vertex model to represent a multi-stage unit with 1-2 connectivity |
CMultiCompressorIntercooled< N > | |
CPressureSwingAbsorption | |
CReboilerCrossFlow | |
CZone | Zone of a vertical shell and tube water steam fed thermosiphon |
CHtuNtu | Vertex model to represent countercurrent multicomponent mass transfer of dilute components in an absorber or a stripper |
CMixer | Vertex model to represent a multi-stream Mixer |
CMultiExchanger | Vertex model to represent an (optionally reactive) rating multi-Stream heat exchanger |
CMultiplier | Vertex model to represent a stream Multiplier |
CSelector | Vertex model to represent a stream Selector |
CSeparator | Vertex model to represent a general purpose separator with many inlets and nOutlets >= 2 outlets |
CSplitter | Vertex model to represent a stream phase separator |
CTerminator | Special purpose model to serve as source or sink of all streams entering a flowsheet and as sink to all stream exiting the flowsheet |
CFlowSheet | |
CCategory | |
►CComponentInterface | |
►CComponentBase | |
►CComponentBiochem | |
Cpurecomps::Ashes | |
Cpurecomps::Carbohydrate | |
Cpurecomps::Fiber | |
Cpurecomps::Lipid | |
Cpurecomps::Protein | |
►CComponentBkk | |
Cpurecomps::CaO | |
Cpurecomps::Fe | |
Cpurecomps::Fe3O4 | |
Cpurecomps::FeO | |
Cpurecomps::silica | |
Cpurecomps::silicon | |
CComponentCmu | |
►CComponentDippr | |
Cpurecomps::BuOH | |
Cpurecomps::CO | |
Cpurecomps::CO2 | |
Cpurecomps::DiethyleneGlycol | |
Cpurecomps::EthyleneGlycol | |
Cpurecomps::Ethylhexanol | |
Cpurecomps::H2 | |
Cpurecomps::MA | |
Cpurecomps::N2 | |
Cpurecomps::NO2 | |
Cpurecomps::O2 | |
Cpurecomps::Octamethyltrisiloxane | |
Cpurecomps::OctylPalmitate | |
Cpurecomps::PalmiticAcid | |
Cpurecomps::TriethyleneGlycol | |
Cpurecomps::aacid | |
Cpurecomps::acetone | |
Cpurecomps::ammonia | |
Cpurecomps::argon | |
Cpurecomps::benzene | |
Cpurecomps::butane | |
Cpurecomps::ciclohexane | |
Cpurecomps::eicosane | |
Cpurecomps::ethane | |
Cpurecomps::ethanol | |
Cpurecomps::ethylene | |
Cpurecomps::etylacetate | |
Cpurecomps::heavy | |
Cpurecomps::helium | |
Cpurecomps::hexene | |
Cpurecomps::hydrogensulfide | |
Cpurecomps::ibutane | |
Cpurecomps::ipentane | |
Cpurecomps::methane | |
Cpurecomps::methanol | |
Cpurecomps::mxylene | |
Cpurecomps::naphthalene | |
Cpurecomps::nbutylene | |
Cpurecomps::ndecane | |
Cpurecomps::nheptane | |
Cpurecomps::nhexadecane | |
Cpurecomps::nhexane | |
Cpurecomps::nnonane | |
Cpurecomps::noctane | |
Cpurecomps::oxylene | |
Cpurecomps::pentane | |
Cpurecomps::phenol | |
Cpurecomps::propane | |
Cpurecomps::propylene | |
Cpurecomps::pxylene | |
Cpurecomps::squalane | |
►CComponentPdippr | |
Cpurecomps::water | |
►CComponentSolid | |
Cpurecomps::CaCO3 | |
Cpurecomps::CaCl2 | |
Cpurecomps::CaF2 | |
Cpurecomps::CaO2H2 | |
Cpurecomps::Fe2O3 | |
Cpurecomps::FeCl2 | |
Cpurecomps::FeF2 | |
Cpurecomps::Na2Hs | |
Cpurecomps::Na2SO4 | |
Cpurecomps::NaCl | |
Cpurecomps::NaF | |
Cpurecomps::NaOH | |
Cpurecomps::Ni | |
Cpurecomps::NiF2 | |
Cpurecomps::Sn | |
Cpurecomps::SnO | |
Cpurecomps::SnO2 | |
Cpurecomps::ZnCl2 | |
Cpurecomps::ZnHs | |
Cpurecomps::ZnS | |
Cpurecomps::ZnSO4 | |
Cpurecomps::ZnSO4H2O | |
Cpurecomps::carbon | |
►CComponentGeneric | |
CComponentBiochem | |
CComponentBkk | |
CComponentCmu | |
CComponentDippr | |
CComponentPdippr | |
CComponentSolid | |
►CRouteHeatVaporCmu | |
CComponentCmu | |
►CRouteTransport | |
CComponentGeneric | |
►CRouteTransportCmu | |
CComponentCmu | |
►CRouteTransportDippr | |
CComponentDippr | |
CComponentPdippr | |
►CRouteTransportDummy | |
CComponentBkk | |
CComponentSolid | |
►CRouteTransportSimple | |
CComponentBiochem | |
CRouteTransportDippr | |
►CRouteVolumeVaporIdeal | |
CComponentCmu | |
►Cdippr | |
CComponentDippr | |
►Cpdippr | |
CComponentPdippr | |
Cdippr | |
Cpdippr | |
CPhase::Activity::ComponentUnifac | |
CNode::ConstIterator | |
CObject::ConstIteratorQuantities | |
CNode::ConstRange | |
CObject::ConstRangeQuantities | |
CCut | |
CCutsSolution | |
CLibpf::Persistency::Defaults | To pass to all informations required during the construction to configure Case instances |
►CDeInterface | Base class for Differential Equations systems solvers |
►CDaeInterface | Base class for Differential Algebraic Equations systems solvers |
CSolverDaeIda | |
►CDiagnostic | |
CAssignment | Used to store an explicit equation |
CComponentGeneric | |
►CFlash | |
►CFlashVl | |
CStreamTwo< FlashVl > | |
►CFlashVlT | |
►CFlashVlTx | |
CFlashLlTx | |
CStreamIapwsLiquidVapor | |
CStreamOne | Stream with a single fluid phase |
CStreamOneSolid | Parameterized stream with a single fluid phase and one solid phase |
CStreamSimple< NV, NL, NS > | |
CHomotopy | |
►CNode | Concrete class, to represent a persistable node belonging to a hierarchical tree structure; the descendant ids are inside a sequential range of ids [rootId() .. (rootId() + range() - 1)] for a Node belonging to a tree the tag must be unique among siblings; also contains properties and methods related to the visualization (icon, setIcon...) |
►CObject | A Node with Quantity, String and Integer variables |
►CModel | |
►CMultiReaction< 2 > | |
CMultiReactionElectrochemical | |
CMultiReactionTransfer | Model for multi reaction with phase transfer |
CEdgeBase | |
►CElectricalConsumption | |
CCompressor | |
CPump | Simple class for liquid pump calculation |
►CFlashDrumBase | |
CFlashDegasser | Parameterized vertex model to represent an (optionally reactive) flash drum with many inlets and two outlets: one vapor phase outlet stream and one liquid / condensate / solid phase outlet stream |
CFlashDrum | |
CFlashSplitter | Parameterized vertex model to represent an (optionally reactive) Flash drum with many inlets and X outlets |
CMultiReaction< N > | Model to represent a generic multiphase Reaction object |
►CPhase::Mass | Phase model interface mass-based only |
►CPhase::MassMolar | Adds molar representation to Mass |
►CPhase::MassMolarProperties | Adds physical properties calculation to MassMolar |
►CPhase::Generic | Parameterizes MassMolarProperties |
►CPhaseGeneric< U > | |
CPhaseActivity< U > | For liquid phases with activity-coefficients thermo |
CPhaseGeneric< T > | Generic phase model with properties and mass / molar representation |
CPhaseTotal | A total phase model Accumulates mass and molar flows over all phases and computes the total phase for a stream |
CPhaseSimple | Simple mass-balance only {vapor, liquid, solid} phase Options: |
CPhaseSimpleTotal | Total phase model for simple mass-balance only (fraction, mdot, w, mdotcomps) Accumulates mass flows over all phases and computes the total phase for a stream |
►CPipeBase | |
CPipe | Model for a pipe object for liquids |
►CRatingColumn | |
►CRatingColumnTray | |
CRatingColumnTraySieve | |
►CRatingHeat | |
►CShellAndTube | Model to represent a Shell and Tube heat exchanger geometry |
►CShellCondensing | |
CRatingHeatShellAndTubeFallingFilmReboiler | |
CRatingHeatShellAndTubeHeater | Model to represent a Shell and Tube heat heater fluid one (process, cold): tube side fluid two (utility, hot): shell side |
CRatingHeatShellAndTubeThermosiphon | Model to represent a Shell and Tube heat Vertical Thermosiphon fluid one (process, cold): tube side fluid two (utility, hot): shell side |
►CShellSensible | |
CRatingHeatShellAndTubeRecovery | Model to represent a Shell and Tube heat heat recovery fluid one (process, cold): tube side fluid two (process, hot): shell side |
►CTubesBoiling | Model to represent Tube-side forced boiling fluid one (process, cold): tube side |
CRatingHeatShellAndTubeThermosiphon | Model to represent a Shell and Tube heat Vertical Thermosiphon fluid one (process, cold): tube side fluid two (utility, hot): shell side |
►CTubesFallingFilmBoiling | Model to represent tube side falling film boiling fluid one (process, cold): tube side |
CRatingHeatShellAndTubeFallingFilmReboiler | |
►CTubesSensible | Model to represent Tube-side single phase sensible heat transfer (heating or cooling) |
CRatingHeatShellAndTubeHeater | Model to represent a Shell and Tube heat heater fluid one (process, cold): tube side fluid two (utility, hot): shell side |
CRatingHeatShellAndTubeRecovery | Model to represent a Shell and Tube heat heat recovery fluid one (process, cold): tube side fluid two (process, hot): shell side |
►CReaction | Model to represent a generic Reaction object |
►CReactionYield | Model to represent a Reaction with specified fixed conversion |
►CReactionEquilibrium | Model to represent a generic Reaction at equilibrium |
CReactionOxidationEquilibriumCH4 | Model to represent the combustion of methane at equilibrium |
CReactionOxidationEquilibriumN2 | Model to represent the oxidation of nitrogen at equilibrium |
CReactionReformingEquilibriumC2H6 | Model to represent the reforming of ethane at equilibrium |
CReactionReformingEquilibriumC3H8 | Model to represent the reforming of propane at equilibrium |
CReactionReformingEquilibriumCH4 | Model to represent the reforming of methane at equilibrium |
CReactionReformingEquilibriumMeOH | Model to represent the reforming of methanol at equilibrium |
CReactionSynthesisEquilibriumNH3 | Model to represent the synthesis of ammonia at equilibrium |
CReactionWaterGasShiftEquilibrium | Model to represent a Water Gas Shift Reaction at equilibrium |
CReactionOxidationC2H6 | Model to represent the total combustion of ethane with specified fixed conversion |
CReactionOxidationCO | Model to represent the total combustion of CO with specified fixed conversion |
►CReactionOxidationHydrocarbon | Model to represent the total combustion of a generic hydrocarbon (CxHy) with specified fixed conversion |
CReactionOxidationEquilibriumCH4 | Model to represent the combustion of methane at equilibrium |
CReactionOxidationMeOH | Model to represent the total combustion of methanol with specified fixed conversion |
►CReactionOxidationN2 | Model to represent the oxidation of nitrogen |
CReactionOxidationEquilibriumN2 | Model to represent the oxidation of nitrogen at equilibrium |
CReactionOxidationNH3 | Model to represent the total combustion of ammonia with specified fixed conversion |
CReactionOxidationPhenol | Model to represent the total combustion of phenol with specified fixed conversion |
►CReactionReformingC2H6 | Model to represent the reforming of ethane with specified fixed conversion |
CReactionReformingEquilibriumC2H6 | Model to represent the reforming of ethane at equilibrium |
►CReactionReformingC3H8 | Model to represent the reforming of propane with specified fixed conversion |
CReactionReformingEquilibriumC3H8 | Model to represent the reforming of propane at equilibrium |
►CReactionReformingCH4 | Model to represent the reforming of methane with specified fixed conversion |
CReactionReformingEquilibriumCH4 | Model to represent the reforming of methane at equilibrium |
►CReactionReformingMeOH | Model to represent the reforming of methanol with specified fixed conversion |
CReactionReformingEquilibriumMeOH | Model to represent the reforming of methanol at equilibrium |
►CReactionSynthesisNH3 | Model to represent the synthesis of ammonia |
CReactionSynthesisEquilibriumNH3 | Model to represent the synthesis of ammonia at equilibrium |
CReactionWaterGasC | Model to represent the water gas production fron C with specified fixed conversion |
►CReactionWaterGasShift | Model to represent a Water Gas Shift Reaction with specified fixed conversion |
CReactionWaterGasShiftEquilibrium | Model to represent a Water Gas Shift Reaction at equilibrium |
►CTabular | Mixin for constant kvli |
CStreamTabularLiquidLiquid | |
CStreamTabularLiquidVapor | |
CVertexBase | Base of the hierarchy of all vertex model types to be included in a FlowSheet This class manages the connection of vertexes with edges and derived classes must implement the Calculatable interface |
►CObjectiveNleInterface | |
CObjectiveFlood | |
CObjectiveLoad | Objective function to determine the load limits |
►CObjectiveNleAuto | Objective function with analytical derivatives computed with FADOO (Forward Automatic Differentiation with Operator Overloading) |
►CObjectiveNleAd | Objective function with scaling based on Scaler class and analytical derivatives computed with FADOO |
CFlash | |
►CObjectiveNleAdVertex | Differentiate calculateResiduals and calculateResidualsLocal |
CCompressor | |
CExchanger | |
CFlashDrumBase | |
CMultiExchanger | Vertex model to represent an (optionally reactive) rating multi-Stream heat exchanger |
►CObjectiveNleAdFlowsheet | Differentiate calculateResiduals and calculateResidualsLocal |
CFlowSheet | |
CSeparator | Vertex model to represent a general purpose separator with many inlets and nOutlets >= 2 outlets |
CObjectiveScalar | Scalar objective function with scaling |
►CPersistency | Pesistent storage management class |
CPersistencyOdbc | Manage the Persistency storage inside ODBC database |
CPersistencyPostgres | Manage the Percistency storage inside Postgres data source |
CPersistencySqlite | Manage the Percistency storage inside SQLite data source |
►CRouteHeatLiquid | |
►CChoiOkos | |
CComponentBiochem | |
CComponentGeneric | |
►CRouteHeatLiquidBkk | |
CComponentBkk | |
►CRouteHeatLiquidDummySolidBkk | |
CComponentSolid | |
Cdippr | |
Cpdippr | |
►CRouteHeatSolid | |
CChoiOkos | |
CComponentGeneric | |
CRouteHeatLiquidDummySolidBkk | |
►CRouteHeatSolidBkk | |
CComponentBkk | |
►CRouteHeatSolidDummy | |
CComponentDippr | |
CComponentPdippr | |
►CRouteHeatVapor | |
CComponentGeneric | |
CRouteHeatVaporCmu | |
►CRouteHeatVaporDippr | |
Cdippr | |
►CRouteHeatVaporDummy | |
CComponentBiochem | |
CComponentBkk | |
CComponentSolid | |
CRouteHeatVaporVolp | |
Cpdippr | |
►CRouteVolumeLiquid | |
CChoiOkos | |
CComponentBkk | |
CComponentGeneric | |
CComponentSolid | |
►CRouteVolumeLiquidDippr | |
Cdippr | |
CRouteVolumeLiquidWater | |
Cpdippr | |
CSensitivity | |
►CSequentialAssembly | Contains informations about cuts and user specified global equations |
CFlowSheet | |
CSolverConjugateGradient | Conjugate Gradient minimization |
►CSolverNleInterface | |
►CAutomatic | |
CSolverNleQAutomatic | |
CSolverNleRecipesAutomatic | |
►CNumeric | |
CSolverNleQNumeric | |
CSolverNleRecipesNumeric | |
►CSolverNleQ | |
CSolverNleQAutomatic | |
CSolverNleQNumeric | |
►CSolverNleRecipes | |
CSolverNleRecipesAutomatic | |
CSolverNleRecipesNumeric | |
CDimension | |
CDirection | |
►CLibpf::Utility::EnumeratorInterface | Abstract interface for static and dynamics enumerators |
CLibpf::Core::Enumerator | Dynamic enumerator, to define the valid values for a StringOption |
CLibpf::Utility::SmartEnumerator< T > | Trait type to define the a static set of valid values for a StringOption |
►CError | |
CErrorBrowsing | |
CErrorConnectivity | |
CErrorDynamicCast | |
CErrorInvalidCharacter | |
CErrorJson | |
CErrorObjectFactory | |
CErrorRunTime | |
CErrorSmartEnum | |
CErrorUnit | |
►CF | |
CStreamTwo< F > | Stream with two fluid phases, use for VL or LL equilibria |
CStreamTwoSolid< F > | Stream with two fluid phases and one solid use for vapor-liquid solid or liquid-liquid-solid streams |
CFactoryFlowsheets | |
CFactoryPhases | |
CFactoryReactions | |
CFactoryStreams | |
CFactoryUnits | |
►CFlashBase | |
CFlash | |
CStream | Edge model for the mass and energy balance of a generic stream semi-abstract class Contains P, T and one Phase subobject: total phase |
CFlashMode | |
►CFlowPattern | |
►CFlowPatternAscii< 6, 6 > | |
CFlowPatternSpiralRight66 | |
►CFlowPatternAscii< 9, 6 > | |
CFlowPatternSpiralRight96 | |
CFlowPatternAscii< NX, NY > | |
CFlowPatternDummy | |
►CFlowPatternSimple< NX, NY > | |
CFlowPatternDown< NX, NY > | FlowPatternDown hardwired flow pattern, Direction=down |
CFlowPatternLeft< NX, NY > | FlowPatternLeft hardwired flow pattern, Direction=left |
CFlowPatternRight< NX, NY > | FlowPatternUp hardwired flow pattern, Direction=right |
CFlowPatternUp< NX, NY > | FlowPatternUp hardwired flow pattern, Direction=up |
CFormulaParser | |
CGenericValue< valuetype > | Model for physical quantities complete with unit of measurement, derivates and persistency |
►CGenericValue< GenericActive< double > > | |
CQuantity | Floating point variable |
►CGroupBkk | |
CRouteHeatLiquidDummySolidBkk | |
►CHomotopyInput | |
CHomotopy | |
CHomotopyInputJson | Initialize from JSON |
CHomotopyInputXml | Initialize from XML file |
CHomotopyVariable | |
CIcon | |
CLibpf::Persistency::IntegerOption | To define the supported integer options within a TypeDescriptor |
CPhase::Generic::Interface | |
►CItem | Semi-abstract class, with a type, a tag and a description; also knows about its parent so can be part of a hierarchical data structure |
►CType< int > | |
CInteger | Integer variable |
►CType< std::vector< int > > | |
►CTypeVector< int > | |
CIntegerVector | Integer vector variable |
►CType< std::vector< Value > > | |
►CTypeVector< Value > | |
CQuantityMatrix | Real matrix variable |
CQuantityVector | Real vector variable |
►CType< std::string > | |
CString | String variable |
►CType< std::vector< std::string > > | |
►CTypeVector< std::string > | |
CStringVector | String vector variable |
►CType< std::vector< T > > | |
CTypeVector< T > | Generic vector Item, header-only |
►CPersistent | Semi-abstract class for Items with an id; can be persisted i.e. serialized |
CNode | Concrete class, to represent a persistable node belonging to a hierarchical tree structure; the descendant ids are inside a sequential range of ids [rootId() .. (rootId() + range() - 1)] for a Node belonging to a tree the tag must be unique among siblings; also contains properties and methods related to the visualization (icon, setIcon...) |
CQuantity | Floating point variable |
CType< T > | Generic Item, header-only |
CNode::Iterator | |
►Cstd::iterator | |
CObject::IteratorQuantities | |
CJacobian | |
CKey | |
CLibpfInitializer | |
CListComponents | Component list manager
Vector Wrapper to manage the actual component list |
CMassBalanceMode | |
►CMonitoredVariable | |
CControlledVariable | |
CMutableVector | |
CNodeFactory | Node factory |
CNodeFactoryInitializer | |
CObjectFactory0< CtorSignature, U > | Object factory for 0 parameter-constructor |
CObjectFactory0< B(void), U > | |
►CObjectiveDae | Abstract base class for defining Differential Algebraic Equation systems |
CObjectiveDaeDynamic | ObjectiveDae derivate to encode the DAE set for the dynamic resolution of a flowsheet |
►CObjectiveScalarInterface | Scalar objective function for optimization |
CObjectiveScalar | Scalar objective function with scaling |
CLibpf::Utility::Option | To define the individual values of an Enumerator |
►COrdering | |
COrderingLexicographical | |
COrderingReflectedGray | |
COrderingSpiral | |
CParameterAntoine | |
CParameterBkk | |
CParameterChoiOkos | |
►CParameterDippr7 | |
Ckldip_parameterWater | |
Ckvdip_parameterWater | |
Cmuldip_parameterWater | |
Cmuvdip_parameterWater | |
Csigdip_parameterWater | |
CParameterHenry | |
CPhase::Activity::ParametersNrtl1 | |
CPhase::Activity::ParametersNrtl2 | |
CPhase::Activity::ParametersUnifac | |
CParameterVolp | |
CPhase::PcsaftParameters | |
CPhaseIndex | |
CPhaseType | |
►CPrecedence | |
CEdgeBase | |
CProduct | |
CLibpf::Persistency::QuantityOption | To define the supported Quantity options within a TypeDescriptor |
CNode::Range | |
CObject::RangeQuantities | |
CRecorder | |
CRegistrar | |
►Cregistry_value | |
Cregistry_int< T > | |
Cregistry_string< T > | |
Cregistry_string< std::basic_string< TCHAR > > | |
CResult | |
►CRouteSaturation | |
CComponentGeneric | |
►CRouteSaturationCmu | |
CComponentCmu | |
►CRouteSaturationDummy | |
CComponentBiochem | |
CComponentBkk | |
CComponentSolid | |
Cdippr | |
Cpdippr | |
►CRouteVolumeSolid | |
CChoiOkos | |
CComponentGeneric | |
►CRouteVolumeSolidDummy | |
CComponentBkk | |
CComponentDippr | |
CComponentPdippr | |
CComponentSolid | |
►CRouteVolumeVapor | |
CComponentGeneric | |
►CRouteVolumeVaporDummy | |
CComponentBiochem | |
CComponentBkk | |
CComponentSolid | |
CRouteVolumeVaporIdeal | |
CScaler | |
CScalingMode | |
►CSensitivityInput | |
CSensitivity | |
CSensitivityInputJson | Initialize from JSON |
CSensitivityInputXml | Initialize from XML file |
►CSensitivityResult | |
CSensitivity | |
►CStreamInterface | |
CStream | Edge model for the mass and energy balance of a generic stream semi-abstract class Contains P, T and one Phase subobject: total phase |
CLibpf::Persistency::StringOption | To define the supported string options within a TypeDescriptor |
►CTask | |
CVertexBase | Base of the hierarchy of all vertex model types to be included in a FlowSheet This class manages the connection of vertexes with edges and derived classes must implement the Calculatable interface |
CTiming | Timer for diagnostic purposes |
►CPhase::Total | |
CPhaseSimpleTotal | Total phase model for simple mass-balance only (fraction, mdot, w, mdotcomps) Accumulates mass flows over all phases and computes the total phase for a stream |
CPhaseTotal | A total phase model Accumulates mass and molar flows over all phases and computes the total phase for a stream |
CLibpf::Persistency::TypeDescriptor | To define the characteristics of a type before a Case of such type is instantiated |
CUnitArrayGen< T > | |
CUnitArrayGen< int > | |
CUnitEngine | Unit of mesurement converter |
CVector | |