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