GMS 2003.11.11 Aspentech An ontology for Computer-Aided Process Engineering (CAPE). Process modeling, simulation, and design 0.8 ConservationLaw ConstructionMaterial CostsForSystemsRealization CompositeProcessStep Combination TemporalDomain LightKeyRecovery ElementarySurface SplittingMaterialPort BehaviorUnitProperty ManagementSystem ServiceFacilityCosts WasteProduct Mixing PhaseEquilibriumLaw ConvectiveMomentumFlux MolecularTransportPhenomenon RawMaterial GeneralMixingSplittingBehavior Plant Shell InterPhaseViscousMomentumTransportLaw Valve PartialMolarVolume HeatRadiationFlux IntraPhaseTransportPhenomenonLaw NonlinearModelSolutionStrategy GlobalFactorialModel LinearModelSolutionStrategy ShapeRepresentation Hybrid EcologicalPerformance ModelPortType Viscosity InterfaceStandard Energy ChemicalSpecies AdsorptionKineticsLaw Point Product DiscreteTimeDomain Height OrdinaryDifferntialModelSolutionStrategy FilmConnection MaterialAmountConnection FlashVaporRatio ReactionEquilibriumConstantModel PhaseComponent ChemicalComponentFraction EquipmentNozzle PlantItemProperty HeatTransferCoefficientTimesArea ValveConnection SurfaceReactionRateCoefficient ScalarQuantity ModelPortTypeElement PressureDrop Length ChemicalReactionPhenomenon ProblemDescription StreamVariable RobustnessRequirement GeneralizedAmount InterDistillationTrayVaporFlowCoupling MassConservationLaw HeatTransferUnit BehavioralPort BehavioralUnit HeatTransferRate RelativeTemporalPoint ViscousMomentumTransportForOneVelocityElement HeatTransferSurface TypeOfInvolvedSteps Radius ChemicalReactionNetwork PipeNozzle MassModel TrayColumn HardwareDevice IntraPhaseMassDiffusionLaw MathematicalModel TubeBundle MassDiffusionCoefficientModel Coupling Equipment DifferentialAlgeraicModel Reaction ChemicalReactionPackage ExtensiveMaterialAmountProperty SpatialCoordinateSystem HeatTransferCoefficient SafetyPerformance Volume ThermalEquilibriumLaw HeatRadiationConnection HeatRadiation ProcessStepProperty ProcessingSubsystemCoupling SystemIdentification PhaseInterfaceHeatConductionFlux HeterogeneousReactionRateCoefficientModel PhaseEquilibriumRatioModel EnergyFlux InstallationCostsForSystemsRealization ShellTubeHeatExchangerEnvironmentCoupling VariablesType IntegerScalarQuantity QuantityCorrespondence Machine PhaseInterfaceMomentumFlux SurfaceTension PopulationConservationLaw ProcessPort ProcessStep CostModel HeatTransferResistance Particle CapacityFCIModel SurfaceReactionProperty CapacityLimitation IndirectInvestment EnthalpyModel SurfaceDiffusionFlux PartialMolarEnthalpyModel OperatingSubsystem DiscreteModel DifferentialModel OutputProduct HeatTransferFilmConnection TrayNumberingConvention SinglePhaseInMultiplePhases ContinuousComposition ProcessingMaterial Fugacity TotalCosts ColumnCosts HomogeneousReactionRateCoefficientModel ContinuousTimeDomain ContinuousMaterialAmount PartialDifferentialAlgebraicModel MultiplePhases PhaseInterfaceMassDiffusionFlux NumericalValueType Results ChemicalReactionRate OpenFormModel HardwareRequirements MaterialAmountConnectionProperty DyadElement IntraPhaseHeatConductionLaw SubmodelDefinition PerformanceCharacteristic ProcessState Process WorkingCapital MainFrame ProcessModel PurchaseCostsForSystemsRealization FlashUnitBehavior SoftwareRequirements GeometricProperty AgglomerationLaw AbsoluteTemporalPoint PhaseBehaviorModel DistillationProcessPort RefluxRatio MixingAndSplitting ConvectiveMaterialFlowLaw ElementaryMaterialAmountConnection ShellTubeHeatExchanger NonEquilibriumAdsorption ParticlePhenomenon InterPhaseMassDiffusionLaw MaterialAmountEnvironmentConnection CondensationMode PhaseInterfaceHeatConduction ValueRange PseudoComponent AdsorptionRateCoefficient PartialMolarEnthalpy BreakageLaw PhaseInterfaceTransportCoefficient VesselCosts ConvectiveMaterialFlow NucleationLaw PerformanceRequirement PhaseInterfaceTransportFlux Apparatus SpatialCoordinateSystemAxis PartialMolarVolumeModel ResourcePrecondition Substance HeatTransferCoefficientModel ConvectiveTransportProperty AdsorptionEquilibriumConstant Box Domain CostsForBuildings AdsorptionRateCoefficientModel DistributionDomain CompositeSurface EnthalpyChange Separation SpecificEnthalpy InterPhaseTransportPropertyModel TemporalDuration PartialDifferentialModel FlowPattern DistillateToFeedRatio ProcessingSubsystem desorptionRateCoefficient FirstPrincipleBased PhaseEquilibriumRatio ModelComponent InterPhaseHeatConductionLaw PlantItem ReactionKineticsLaw EnergyAccumulation ShellTubeHeatExchangerShellSideMaterialAmount PhaseSystemCondition ModelingTaskSpec ExtensiveThermodynamicState SpecificVolume PropertyValueSupport MomentumAccumulation ChemicalReaction PressureChangeOfGas MaterialQuantityBasis SolverComponent PhaseInterfaceTransportPhenomenon ContinuousModel CPProperty ChemicalReactorBehavior AdsorptionPhenomenon Circle PropertyModelPair CompositeShapeRepresentation AdsorptionEquilibriumConstantModel DispersedMaterialAmount ParticulateStateDomain FlashUnit RecycleStructure SixTenthsRuleModel IntensiveMaterialAmountProperty StateVariableGradient DiscreteComposition ChemicalProcessMaterial AdsorptionProperty ChemicalKineticsLaw SphericCoordinateSystem IntraPhaseTransportPropertyModel SpatialDomain ModelingPrinciple PhaseInterfaceTransportProperty SoftwareInterface Distillation EquipmentCosts ReactionRateCoefficient FluxDirectionElement PhaseComponentProperty DistillationTrayBehavior PackedColumn SurfaceReactionEquilibriumConstant MassTransferCoefficient RealScalarQuantity Agglomeration NumericsComponent GenericCoordinateSystem EquilibriumChemicalReaction KeyChemicalComponentConversionRatio Cone TemporalPoint ConvectiveFlowVelocity PMC PME ParticlePopulationAccumulation TurbulentFlow ConvectiveEnergyFlux AggregationState GeneralMixingSplittingMaterialAmount PhysicalContext DomainType EquilibriumAdsorption ModelVariableType DensityModel 3DVectorQuantity MultistepMethod AlgeraicModel PerformanceModel FugacityCoefficientModel Sphere FilmConnectionPort ChemicalReactionEquilibriumLaw SpeedRequirement CharacteristicSize ResourceConstraint SingleComputerRequirements SurfaceReactionRate ShellTubeHeatExchangerOneSideMaterialAmount DistillationSystemBehavior ChemicalProcessMaterialProperty ChemicalComponentConstant FeedTank ChemicalKineticsPropertyModel MomentumFlux Stirrer EquationOfStateModel DetailedItemFCIModel IntensiveThermodynamicStateModel Activity PhysicalEquilibrium PhaseInterfaceViscousMomentumTransport QualitativeValue ModelPortDefinition PhaseEquilibrium PhenomenonLawPair ProblemClarification InterDistillationTrayLiquidFlowCoupling ModelSolutionStrategy DifferentialAlgebraicModelSolutionStrategy InternetConnection ConceptualSolution VectorElement VesselOrientation PurposeOfModeling By-product ResourceParameterInitialization PropertyValue TemperatureChange ThermoModel Rectangle ExplicitMethod GibbsFreeEnergyModel ThermalEquilibrium DistillationColumn ProductionCosts Pressure TransportPhenomenaProperty ShellTubeHeatExchangerShellTubeCoupling DesignRationale Value IntermediateProduct SinglePhase TransportPhenomenonLaw ChemicalProcessSystemPerformance PieceOfEquipment PipeCosts ModelVariableDefinition ShellTubeHeatExchangerShellTubeMaterialAmountConnection 3DDyadQuantity ConvectiveMassFlux VolumeModel CountingProperty InstrumentationCosts ModelingRequirements ManufacturingCosts EquationSystemType DistillationColumnBehavior Surface TypeOfExplicitness Reactant Leaching LaminarFlow TurnoverRatioModel ProblemStatement PhaseChange ShellTubeHeatExchangerOneSideMaterialAmountEnvironmentConnection Property Flashing ChemicalComponent FactorialFCIModel NonEquilibriumChemicalReaction NonEquilibriumContext Growth MomentumConservationLaw PowerFactorModel UnitCostEstimateModel EnvironmentTerminal ThermoComponent ChemicalProcessSystem OrthogonalCoordinateSystem MassDiffusion ActivityCoefficient PhaseSystemProperty NonEquilibriumLaw PhaseSystem NonReusableWasteProduct HeatConductivity ThermodynamicStateProperty GrowthLaw MassTransferCoefficientModel Area Flux Mass PhaseRatio EquilibriumSurfaceReaction ChemicalReactor PhaseInterfaceMassDiffusion ConceptualSolutionAlternatives MaterialAmountProperty DistillationSystem ExtensivematerialAmountPropertyModel CSG-Primitive ThermalConductivityModel IntraPhaseTransportCoefficient FugacityCoefficient DirectInvestment ReusableWasteProduct Column Co-product PressureChangeOfLiquid PressureChange ProductTank WellMixed CostsForLand DiffusionCoefficient ChemicalReactionEquilibriumConstant ShellTubeHeatExchangerTubeSideMaterialAmount Fixture MagnitudeBounds VelocityGradient MaterialAmountConnectionFlowVelocity Result ActivityCoefficientModel SpecificGibbsFreeEnergy Law Permeability MaterialAmount EndProduct Jacket SurfaceTensionModel GroupOfEquipment ParticleKineticsLaw TemaShellType ModelRepresentationForm TotalCapitalInvestment CylindricCoordinateSystem MaterialAmountPhenomenon MaterialModelComponent MechanicalEquilibriumLaw EnergyConservationLaw EquilibriumLaw ViscosityModel SurfaceMassDiffusion ShellTubeHeatExchangerFunction IntraPhaseMomentumTransportLaw Nozzle AdsorptionEquilibriumLaw SurfaceMassDiffusionLaw SurfaceReactionPhenomenon NonEquilibriumSurfaceReaction Splitting Mixture MaterialAmountEnvironmentHeatTransferConnection OneStepMethod Price FixedCapitalInvestment Flow AccuracyRequirement SpecificEnthalpyModel ResourceDescription PartialSolution GeneralExpense OperatingSystem DistributionApproach AlgebraicModelSolutionStrategy Composition ChemicalReactionProperty MassAccumulation ShellTubeHeatExchangerBehavior HeatConduction PropertyModel ValveConnectionPort CPPerformanceProperty ChemicalProduct MixedModel Nucleation HeatRadiationLaw MaterialAmountConnectionPhenomenon InterPhaseProperty ParticleNumber Diameter Vessel Temperature MiddlewarePlatform MechanicalEquilibrium SpatialCoordinate ValueEnumeration ClosedFormModel OrdinaryDifferentialModel UnitOfMeasurement InterPhaseTransportPhenomenonLaw SoftwareSystem ElementaryMaterialAmount Vendor ImplicitMethod GeneralMixingSplittingUnit DataDriven Pipe Pump Tray Tube CurvilinearCoordinateSystem Density MaterialStream Condenser Quantity DifferentialFactorialModel Solution HeatCapacityModel ChemicalComponentConcentration CartesianCoordinateSystem Breakage Distribution HeatRadiationConnectionPort PhysicochemicalPhenomenon InputProduct StepCountingModel AverageParticleState FixedCapitalInvestmentModel Cylinder PhysicalDomain ShellTubeApparatus Accumulation VapourPressureModel ProblemDefinition HeavyKeyRecovery CoreProduct ElementaryShapeRepresentation BehavioralUnitCoupling AdsorptionRate ViscousMomentumTransport TemaClass GeneralMixingSplittingFunction has_fraction_value has_connected_environment_terminal_valve_connection_port averages_particle_state has_property_value_upper_bound includes_partial_solution has_modeled_object_quantity has_involved_phenomenon has_distribution_media is_composed_of_processing_subsystem is_in_non_reaction_equilibrium is_equilibrium_state_of_reaction has_tube_side_bulk_film_coefficient has_standard_version has_model_variable_type has_vector_element has_tray_vapor_inlet_port has_hardware_device has_plant_item_property has_reboiler has_purpose has_condenser_outlet_spliter has_fixed_upper_bound has_distribution_domain has_outlet_port_count has_type_of_involved_steps is_derived_from_phase_behavor_model has_stream_variable has_material_amount_connection_property has_reference_coordinate_system has_problem_description has_processing_subsystem has_outlet_material_port has_connection_speed_lower_limit has_ranking_criterion has_substance_identifier corresponds_to_spatial_axis has_initial_value has_resource_software_description has_solution has_realization_element has_model_variable has_modeling_principle has_outlet_splitting_material_port is_well_formed has_heat_duty is_part_of implements_process_model has_process_model_quantity has_hole_diameter has_material_amount_phenomenon has_bottom_area has_heat_leak_or_loss_port has_inlet_material_port has_length has_vapour_ratio is_of_model_variable_type has_axis_1 has_axis_2 has_axis_3 has_lower_bound has_phase_system has_lower_limit has_raw_material has_extreme_heat_leak_flow has_reference_inter_tray_liquid_flow_coupling is_materialized_by includes_processing_unit has_vendor_digital_signature has_distillation_top_pressure has_stirrer has_length_x has_length_y has_length_z has_dae_linearity has_bulk_flow_direction_element has_radius has_convection_flow_direction is_connection_involved_in_coupling has_unit_of_measurement is_at_process_port has_physical_context has_starting_temporal_point has_value has_line_chemical_formula has_tube_side_environment_connection has_shell_side_wall_film_coeffficient has_system_identification has_interface_name has_capacity_limitation_value has_flux_direction_element has_process_step_property has_design_rationale has_heated_length has_aggregation_state refers_to_phase_system_property has_identification_string has_support has_recycle_structure has_spatial_dimension has_composition has_outlet_material_port_count has_operatingSubsystem has_shell_side_inlet_port has_number_of_trays has_number_of_tubes has_port has_discretisation_interval has_connected_process_port has_phase_component has_particle_accumulation implements_model_solution_strategy has_behavioral_port has_heat_leak has_heat_loss is_non_equlibrium_state_of_reaction has_reference_tray_behavior has_shape_representation Surrounds has_standard_name has_spatial_coordinate_value has_light_key_chemical_component has_chemical_process_property is_able_to_handle_dae_explicitness corresponds_to_generalized_amount has_problem_statement has_constructing_material has_upper_limit has_cyclinder_orientation is_catalyst_required is_able_to_handle_dae_linearity has_capacity_limitation has_property_to_be_specified has_weir_height single_phase_one single_phase_two has_inside_diameter has_spatial_coordinate has_capacity_limitation_item is_managed_by has_particle_phenomenon has_reference_temporal_point has_domain_type is_of_chemical_process_system includes_individual_result has_distribution is_composed_of_value has_input has_surface_geometry has_value_range has_modeling_requirements has_middleware_platform is_composed_of_plant_item has_dyad_element has_number_of_tube_passes_per_shell refers_to_property has_chemical_component has_heat_loss_flow has_middleware_platform_name is_port_involved_in_coupling has_model_representation_form has_material_amount_connection has_processing_subsystem_coupling has_vendor is_in_engineering_stage has_unit_of_measurement has_tube_side_inlet_port has_inlet_model_port has_constants has_number_of_components is_runable_on_operating_system models_phenomenon has_reactant has_pressure_difference has_submodel_definition has_normal_reaction_pressure has_external_area has_phase_component_property has_tube_side_fouling_resistance has_tray_area has_fixture has_inlet_material_port_count has_column_condenser_coupling is_defined_in_standard has_type_of_explicitness models_property has_phase_system_condition has_single_computer_requirements is_at_numbered_tray has_chemical_reaction has_connection_means has_stero_chemical_formula has_heat_conduction_port has_pressure_drop has_power applies_ae_strategy has_numerical_value_type is_complete has_tray_vapor_outlet_port is_coupled_with is_compliant_to_standard has_reference_inlet_material_port corresponds_to_particulate_state has_condenser_spliter_coupling has_spatial_dimension_1 has_spatial_dimension_2 has_permeable_chemical_component requires_supporting_software_system has_distribution_domain has_column has_outlet_model_port has_variable_upper_bound has_property_value_element has_reference_particle has_vendor_name has_adsorbed_chemical_component implements_interface has_aggregation_state has_shell_side_environment_connection has_coupling has_side_area has_resource_constraint has_heat_leak_flow has_tube_side_thermal_resistance has_pump_efficiency has_operating_system_version has_shell_side_bulk_film_coefficient has_magnitude has_shell_side_fouling_resistance has_involved_property_model has_quantity_correspondence has_involved_property has_system_origin has_resource_performance_model has_tray_liquid_inlet_port has_material_amount has_model_port has_model_type is_able_to_handle_dae_index has_height has_memory_size_lower_limit has_characteristic_value has_conceptual_solution is_composed_of_process_step has_column_spliter_coupling has_key_chemical_component has_hard_disk_capacity_lower_limit has_jacket has_resource_parameter_initialization has_CPU_speed_lower_limit has_nonequilibrium_context has_processed_stream is_part_of_material_amount has_property_value has_nozzle has_normal_reaction_temperature has_tube_environment_coupling has_effective_area has_reference_inter_tray_vapor_flow_coupling has_physical_quantity_basis has_time_duration_value is_modeled_by is_owned_by includes_material_stream has_distillation_bottom_pressure has_identification_type is_composed_of_behavior_unit is_in_reaction_equilibrium has_equation_system_type has_resource_description has_stoichiometric_value has_splitting_ratio has_shell_side_thermal_resistance has_volume has_condenser has_behavioral_element corresponds_to_behavioral_port has_internet_connection has_resource_precondition has_delivery_time has_functional_element has_behavioral_unit_property is_port_of_behavioral_unit is_of_model_port_type has_area_xy has_area_xz has_area_zy refers_to_chemical_process_material has_reference_outlet_material_port has_feed_to_tray corresponds_to_model_port_type_element has_element has_dae_explicitness is_inlet_of has_connecting_material_amount_connection has_domain_lower_bound includes_phase_system_property has_single_phase has_performance_requirement has_modeled_object has_heavy_key_chemical_component has_differential_order has_pump_head has_phase_system has_chemical_reaction_network refers_to_chemical_reaction applies_ode_strategy has_tube_side_wall_film_coefficient has_ending_temporal_point is_of_axis has_reference_chemical_component_fraction accomodates_pmc has_physical_dimension has_variables_type has_ratio has_connected_behavioral_port has_physical_dimension has_hardware_requirements has_reference_tube_bundle is_runable_on_middleware_platform has_specification_type has_shell_environment_coupling has_spatial_direction_element has_model_solution_strategy corresponds_to_single_phase includes_processing_subsytem_coupling has_element_identifier has_proportional_heat_loss_flow is_for_engineering_task has_distribution_approach has_characterisic_item has_behavioral_unit_coupling has_number_of_shells_in_series has_performance_characteristic has_physicochemical_mechanism has_overall_heat_transfer_coefficient corresponds_to_chemical_component has_reacting_material_amount has_chemical_component_fraction has_price has_product has_bottom_product_port has_geometry has_phase_system_property has_material_amount_property models_costs has_chemical_reaction_network has_number_of_shells_in_parallel has_domain_upper_bound has_version belongs_to_multiple_phases has_middleware_platform_version supports_interface has_modeling_requirements has_property has_outside_diameter has_preferred_mechanism has_dae_index resides_in has_non_reacting_material_amount has_cone_orientation has_property_to_be_evaluated has_platform_bits has_tube_side_outlet_port has_permeability has_unprocessed_stream has_reference_shell has_output has_pump_capacity has_top_product_port has_reference_tray has_reference_tube has_vendor_contact has_property_value_lower_bound refers_to_substance has_splitting_ratio has_averaged_property has_coordinate_system has_product has_product_from_tray has_material_amount_connection_phenomenon has_transport_for_one_velocity_element has_TEMA_shell_type has_product has_chemical_process_material has_price_value has_time_value has_operating_system_name has_applicable_aggregation_state has_process_state has_inlet_port_count contains_particle has_geometric_property has_vendor_website is_outlet_of has_distribution_mode has_cost_part has_model has_orientation has_vendor_electronic_mail has_TEMA_class has_problem_clarification has_numerical_value has_tray has_tube is_dispersed_in has_proportional_heat_leak_flow has_substance has_distribution_URL has_preselected_pme has_extreme_heat_loss_flow has_column_reboiler_coupling has_tray_liquid_outlet_port is_of_equipment models_object has_shell_side_outlet_port is_associated_to_distribution_approach has_phenomenon has_preferred_property_model has_connecting_material_stream corresponds_to_model_variable_definition has_involved_law has_ode_stiffness includes_chemical_reaction has_crossing_area