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Namespace Enums
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Public Class Dynamics
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Public Enum DynamicsSpecType
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|
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Pressure = 0
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Flow = 1
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End Enum
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Public Enum DynamicsEventType
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|
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ChangeProperty = 0
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RunScript = 1
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End Enum
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Public Enum DynamicsAlarmType
|
|
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LL = 0
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L = 1
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H = 2
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HH = 3
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End Enum
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Public Enum DynamicsEventTransitionType
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|
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StepChange = 0
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LinearChange = 1
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LogChange = 3
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InverseLogChange = 4
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RandomChange = 5
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End Enum
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Public Enum DynamicsEventTransitionReferenceType
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|
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InitialState = 0
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PreviousEvent = 1
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SpecificEvent = 2
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End Enum
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End Class
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Public Class Helpers
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Public Shared Function GetEnumType(typename As String) As Type
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Return Reflection.Assembly.GetExecutingAssembly().GetType(typename)
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End Function
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End Class
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Public Class Scripts
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Public Enum Interpreter
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IronPython = 0
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Python_NET = 1
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End Enum
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Public Enum ObjectType
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Simulation = 0
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Solver = 1
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FlowsheetObject = 2
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Integrator = 3
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End Enum
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Public Enum EventType
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|
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SimulationOpened = 0
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SimulationSaved = 1
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SimulationClosed = 2
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ObjectCalculationStarted = 3
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ObjectCalculationFinished = 4
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ObjectCalculationError = 5
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SolverStarted = 6
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SolverFinished = 7
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|
|
SolverRecycleLoop = 8
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|
|
SimulationTimer1 = 9
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SimulationTimer5 = 10
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|
SimulationTimer15 = 11
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SimulationTimer30 = 12
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SimulationTimer60 = 13
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IntegratorStarted = 14
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IntegratorFinished = 15
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IntegratorError = 16
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IntegratorStep = 17
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|
IntegratorPreStep = 18
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End Enum
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End Class
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Public Enum SampleType
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|
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Light = 0
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Average = 1
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Heavy = 2
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End Enum
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|
|
Public Enum UndoRedoActionType
|
|
|
SimulationObjectPropertyChanged = 0
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|
|
FlowsheetObjectPropertyChanged = 1
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|
|
FlowsheetObjectConnected = 2
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|
|
FlowsheetObjectDisconnected = 3
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|
|
ObjectAdded = 4
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|
|
ObjectRemoved = 5
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|
|
SystemOfUnitsAdded = 6
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|
|
SystemOfUnitsRemoved = 7
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|
|
SystemOfUnitsChanged = 8
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|
|
CompoundAdded = 9
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|
|
CompoundRemoved = 10
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|
|
PropertyPackagePropertyChanged = 11
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|
|
PropertyPackageAdded = 12
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|
|
PropertyPackageRemoved = 13
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|
|
CutObjects = 14
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|
PasteObjects = 15
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|
|
SpreadsheetCellChanged = 16
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|
|
End Enum
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|
|
Public Enum SnapshotType
|
|
|
All = 0
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|
|
ObjectLayout = 1
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|
|
ObjectData = 2
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|
|
Compounds = 3
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|
|
ReactionSubsystem = 4
|
|
|
PropertyPackages = 5
|
|
|
Spreadsheet = 6
|
|
|
SimulationSettings = 7
|
|
|
WindowLayout = 8
|
|
|
ObjectAddedOrRemoved = 9
|
|
|
End Enum
|
|
|
|
|
|
Public Enum FlowsheetUtility
|
|
|
PhaseEnvelope = 0
|
|
|
PhaseEnvelopeBinary = 1
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|
|
PhaseEnvelopeTernary = 2
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|
|
NaturalGasHydrates = 3
|
|
|
TrueCriticalPoint = 4
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|
|
PSVSizing = 5
|
|
|
SeparatorSizing = 6
|
|
|
PetroleumProperties = 7
|
|
|
PureCompoundProperties = 8
|
|
|
End Enum
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|
|
|
|
|
Public Enum UnitOfMeasure
|
|
|
|
|
|
accel = 0
|
|
|
activity = 1
|
|
|
activityCoefficient = 2
|
|
|
area = 3
|
|
|
boilingPointTemperature = 4
|
|
|
cakeresistance = 5
|
|
|
cinematic_viscosity = 6
|
|
|
compressibility = 7
|
|
|
compressibilityFactor = 8
|
|
|
deltaP = 9
|
|
|
deltaT = 10
|
|
|
density = 11
|
|
|
diameter = 12
|
|
|
distance = 13
|
|
|
enthalpy = 14
|
|
|
entropy = 15
|
|
|
excessEnthalpy = 16
|
|
|
excessEntropy = 17
|
|
|
force = 18
|
|
|
foulingfactor = 19
|
|
|
fugacity = 20
|
|
|
fugacityCoefficient = 21
|
|
|
gor = 22
|
|
|
head = 23
|
|
|
heat_transf_coeff = 24
|
|
|
heatCapacityCp = 25
|
|
|
heatCapacityCv = 26
|
|
|
heatflow = 27
|
|
|
idealGasHeatCapacity = 28
|
|
|
jouleThomsonCoefficient = 29
|
|
|
kvalue = 30
|
|
|
logFugacityCoefficient = 31
|
|
|
logKvalue = 32
|
|
|
mass = 33
|
|
|
mass_conc = 34
|
|
|
massflow = 35
|
|
|
massfraction = 36
|
|
|
mediumresistance = 37
|
|
|
meltingTemperature = 38
|
|
|
molar_conc = 39
|
|
|
molar_enthalpy = 40
|
|
|
molar_entropy = 41
|
|
|
molar_volume = 42
|
|
|
molarflow = 43
|
|
|
molarfraction = 44
|
|
|
molecularWeight = 45
|
|
|
pressure = 46
|
|
|
reac_rate = 47
|
|
|
reac_rate_heterog = 48
|
|
|
spec_vol = 49
|
|
|
speedOfSound = 50
|
|
|
surfaceTension = 51
|
|
|
temperature = 52
|
|
|
thermalConductivity = 53
|
|
|
thermalConductivityOfLiquid = 54
|
|
|
thermalConductivityOfVapor = 55
|
|
|
thickness = 56
|
|
|
time = 57
|
|
|
vaporPressure = 58
|
|
|
velocity = 59
|
|
|
viscosity = 60
|
|
|
viscosityOfLiquid = 61
|
|
|
viscosityOfVapor = 62
|
|
|
volume = 63
|
|
|
volumetricFlow = 64
|
|
|
diffusivity = 65
|
|
|
none = 66
|
|
|
conductance = 67
|
|
|
heat = 68
|
|
|
mole = 69
|
|
|
emission_factor = 70
|
|
|
specificpower = 71
|
|
|
|
|
|
End Enum
|
|
|
|
|
|
Public Enum OptimizationMethod
|
|
|
Limited_Memory_BGFS = 0
|
|
|
Truncated_Newton = 1
|
|
|
Simplex = 2
|
|
|
IPOPT = 3
|
|
|
End Enum
|
|
|
|
|
|
Public Enum AccelMethod
|
|
|
None
|
|
|
Wegstein
|
|
|
Dominant_Eigenvalue
|
|
|
GlobalBroyden
|
|
|
End Enum
|
|
|
|
|
|
Public Enum FlashMethod
|
|
|
Default_Algorithm = 0
|
|
|
Nested_Loops_VLE = 1
|
|
|
Nested_Loops_VLLE = 2
|
|
|
Nested_Loops_Immiscible_VLLE = 3
|
|
|
Inside_Out_VLE = 4
|
|
|
Inside_Out_VLLE = 5
|
|
|
Gibbs_Minimization_VLE = 6
|
|
|
Gibbs_Minimization_VLLE = 7
|
|
|
Simple_LLE = 8
|
|
|
Nested_Loops_SLE_Eutectic = 9
|
|
|
Nested_Loops_SLE_SolidSolution = 10
|
|
|
BlackOil = 11
|
|
|
Electrolyte = 12
|
|
|
SeaWater = 13
|
|
|
SourWater = 14
|
|
|
CAPE_OPEN_Equilibrium_Server = 15
|
|
|
SteamTables = 16
|
|
|
Nested_Loops_SVLLE = 17
|
|
|
CoolProp_Incompressibles = 18
|
|
|
CoolProp_IncompressibleMixtures = 19
|
|
|
UserDefined = 20
|
|
|
Gibbs_Minimization_Multiphase = 21
|
|
|
Universal = 22
|
|
|
Custom = 23
|
|
|
End Enum
|
|
|
|
|
|
Public Enum FlashSetting
|
|
|
|
|
|
PTFlash_External_Loop_Tolerance = 0
|
|
|
PTFlash_Internal_Loop_Tolerance = 1
|
|
|
PTFlash_Maximum_Number_Of_External_Iterations = 2
|
|
|
PTFlash_Maximum_Number_Of_Internal_Iterations = 3
|
|
|
|
|
|
PHFlash_Internal_Loop_Tolerance = 4
|
|
|
PHFlash_External_Loop_Tolerance = 5
|
|
|
PHFlash_Maximum_Number_Of_Internal_Iterations = 6
|
|
|
PHFlash_Maximum_Number_Of_External_Iterations = 7
|
|
|
|
|
|
ThreePhaseFlashStabTestSeverity = 8
|
|
|
ThreePhaseFlashStabTestCompIds = 9
|
|
|
|
|
|
CalculateBubbleAndDewPoints = 10
|
|
|
|
|
|
ValidateEquilibriumCalc = 11
|
|
|
ValidationGibbsTolerance = 12
|
|
|
|
|
|
UsePhaseIdentificationAlgorithm = 13
|
|
|
|
|
|
Replace_PTFlash = 14
|
|
|
|
|
|
GM_OptimizationMethod = 15
|
|
|
|
|
|
IO_FastMode = 16
|
|
|
|
|
|
NL_FastMode = 17
|
|
|
|
|
|
PVFlash_TemperatureDerivativeEpsilon = 18
|
|
|
PVFlash_MaximumTemperatureChange = 19
|
|
|
PVFlash_FixedDampingFactor = 20
|
|
|
|
|
|
ST_Number_of_Random_Tries = 21
|
|
|
|
|
|
CheckIncipientLiquidForStability = 22
|
|
|
|
|
|
PHFlash_MaximumTemperatureChange = 23
|
|
|
|
|
|
PTFlash_DampingFactor = 24
|
|
|
|
|
|
ForceEquilibriumCalculationType = 25
|
|
|
|
|
|
ImmiscibleWaterOption = 26
|
|
|
|
|
|
HandleSolidsInDefaultEqCalcMode = 27
|
|
|
|
|
|
UseIOFlash = 28
|
|
|
|
|
|
GibbsMinimizationExternalSolver = 29
|
|
|
|
|
|
GibbsMinimizationExternalSolverConfigData = 30
|
|
|
|
|
|
PHFlash_Use_Interpolated_Result_In_Oscillating_Temperature_Cases = 31
|
|
|
|
|
|
PVFlash_TryIdealCalcOnFailure = 32
|
|
|
|
|
|
|
|
|
FailSafeCalculationMode = 33
|
|
|
|
|
|
PVFlash_FivePointStencilNumericalDerivative = 34
|
|
|
|
|
|
End Enum
|
|
|
|
|
|
Public Enum FlashCalculationType
|
|
|
PressureTemperature = 0
|
|
|
PressureEnthalpy = 1
|
|
|
PressureEntropy = 2
|
|
|
TemperatureEnthalpy = 3
|
|
|
TemperatureEntropy = 4
|
|
|
PressureVaporFraction = 5
|
|
|
TemperatureVaporFraction = 6
|
|
|
PressureSolidFraction = 7
|
|
|
TemperatureSolidFraction = 8
|
|
|
VolumeTemperature = 9
|
|
|
VolumePressure = 10
|
|
|
VolumeEnthalpy = 11
|
|
|
VolumeEntropy = 12
|
|
|
End Enum
|
|
|
|
|
|
Public Enum AdjustVarType
|
|
|
Manipulated = 0
|
|
|
Controlled = 1
|
|
|
Reference = 2
|
|
|
None = 3
|
|
|
End Enum
|
|
|
|
|
|
Public Enum SpecVarType
|
|
|
Source = 0
|
|
|
Target = 1
|
|
|
None = 2
|
|
|
End Enum
|
|
|
|
|
|
Public Enum PropertyType
|
|
|
RO = 0
|
|
|
RW = 1
|
|
|
WR = 2
|
|
|
ALL = 3
|
|
|
End Enum
|
|
|
|
|
|
Public Enum StreamType
|
|
|
Feed = 0
|
|
|
Product = 1
|
|
|
Recycle_In = 2
|
|
|
Recycle_Out = 3
|
|
|
Inner = 4
|
|
|
Undefined = 5
|
|
|
End Enum
|
|
|
|
|
|
Public Enum StreamSpec
|
|
|
Temperature_and_Pressure = 0
|
|
|
Pressure_and_Enthalpy = 1
|
|
|
Pressure_and_Entropy = 2
|
|
|
Pressure_and_VaporFraction = 3
|
|
|
Temperature_and_VaporFraction = 4
|
|
|
Pressure_and_SolidFraction = 5
|
|
|
Volume_and_Temperature = 6
|
|
|
Volume_and_Enthalpy = 7
|
|
|
Volume_and_Entropy = 8
|
|
|
End Enum
|
|
|
|
|
|
Public Enum FlowSpec
|
|
|
Mass = 0
|
|
|
Mole = 1
|
|
|
Volumetric = 2
|
|
|
End Enum
|
|
|
|
|
|
Public Enum CompositionBasis
|
|
|
Molar_Fractions
|
|
|
Mass_Fractions
|
|
|
Volumetric_Fractions
|
|
|
Molar_Flows
|
|
|
Mass_Flows
|
|
|
Volumetric_Flows
|
|
|
DefaultBasis
|
|
|
End Enum
|
|
|
|
|
|
Public Enum PhaseLabel
|
|
|
Mixture
|
|
|
Vapor
|
|
|
LiquidMixture
|
|
|
Liquid1
|
|
|
Liquid2
|
|
|
Liquid3
|
|
|
Aqueous
|
|
|
Solid
|
|
|
End Enum
|
|
|
|
|
|
Public Enum PhaseName
|
|
|
Liquid
|
|
|
Vapor
|
|
|
Mixture
|
|
|
Solid
|
|
|
End Enum
|
|
|
|
|
|
Public Enum ForcedPhase
|
|
|
None
|
|
|
Vapor
|
|
|
Liquid
|
|
|
Solid
|
|
|
GlobalDef
|
|
|
End Enum
|
|
|
|
|
|
Public Enum ReactionType
|
|
|
Equilibrium
|
|
|
Kinetic
|
|
|
Heterogeneous_Catalytic
|
|
|
Conversion
|
|
|
End Enum
|
|
|
|
|
|
Public Enum ReactionBasis
|
|
|
Activity
|
|
|
Fugacity
|
|
|
MolarConc
|
|
|
MassConc
|
|
|
MolarFrac
|
|
|
MassFrac
|
|
|
PartialPress
|
|
|
End Enum
|
|
|
|
|
|
Public Enum ReactionPhase
|
|
|
Liquid
|
|
|
Vapor
|
|
|
Mixture
|
|
|
Solid
|
|
|
Liquid_Solid
|
|
|
Vapor_Solid
|
|
|
End Enum
|
|
|
|
|
|
Public Enum ReactionKineticType
|
|
|
Arrhenius = 0
|
|
|
UserDefined = 1
|
|
|
End Enum
|
|
|
|
|
|
Public Enum ReactionKinetics
|
|
|
Expression = 0
|
|
|
PythonScript = 1
|
|
|
End Enum
|
|
|
|
|
|
Public Enum KOpt
|
|
|
Gibbs = 0
|
|
|
Expression = 1
|
|
|
Constant = 2
|
|
|
End Enum
|
|
|
|
|
|
Public Enum WarningType
|
|
|
Ignore = 0
|
|
|
ShowWarning = 1
|
|
|
RaiseError = 2
|
|
|
End Enum
|
|
|
|
|
|
Public Enum ListPosition
|
|
|
Top = 0
|
|
|
TopRight = 1
|
|
|
Right = 2
|
|
|
RightBottom = 3
|
|
|
Bottom = 4
|
|
|
BottomLeft = 5
|
|
|
Left = 6
|
|
|
LeftTop = 7
|
|
|
End Enum
|
|
|
|
|
|
Public Enum SimulationObjectClass
|
|
|
|
|
|
Streams = 0
|
|
|
PressureChangers = 1
|
|
|
Separators = 2
|
|
|
MixersSplitters = 3
|
|
|
Exchangers = 4
|
|
|
Reactors = 5
|
|
|
Columns = 6
|
|
|
Solids = 7
|
|
|
CAPEOPEN = 8
|
|
|
UserModels = 9
|
|
|
Logical = 10
|
|
|
Other = 11
|
|
|
Indicators = 12
|
|
|
Controllers = 13
|
|
|
Switches = 14
|
|
|
Inputs = 15
|
|
|
None = 16
|
|
|
CleanPowerSources = 17
|
|
|
Electrolyzers = 18
|
|
|
|
|
|
End Enum
|
|
|
|
|
|
Public Enum ReportItemType
|
|
|
|
|
|
Label = 0
|
|
|
Description = 1
|
|
|
TripleColumn = 2
|
|
|
DoubleColumn = 3
|
|
|
SingleColumn = 4
|
|
|
|
|
|
End Enum
|
|
|
|
|
|
Public Enum ReportType
|
|
|
|
|
|
PlainText = 0
|
|
|
RichText = 1
|
|
|
Structured = 2
|
|
|
|
|
|
End Enum
|
|
|
|
|
|
Public Enum CompoundOrdering
|
|
|
|
|
|
AsAdded = 0
|
|
|
Name_ASC = 1
|
|
|
Name_DESC = 2
|
|
|
NBP_ASC = 3
|
|
|
NBP_DESC = 4
|
|
|
MW_ASC = 5
|
|
|
MW_DESC = 6
|
|
|
CAS_ASC = 7
|
|
|
CAS_DESC = 8
|
|
|
TAG_ASC = 9
|
|
|
TAG_DESC = 10
|
|
|
|
|
|
End Enum
|
|
|
|
|
|
Public Enum ChartType
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TwoDimensionalScatter = 0
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Pie = 1
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HorizontalBars = 2
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VerticalBars = 3
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End Enum
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Public Enum ChartSource
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SpreadsheetRange = 0
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FlowsheetObject = 1
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End Enum
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Public Enum ExtenderLevel
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MainWindow = 0
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FlowsheetWindow = 1
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End Enum
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Public Enum ExtenderCategory
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File = 0
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Edit = 1
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Settings = 2
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Tools = 3
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Utilities = 4
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Dynamics = 5
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Optimization = 6
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Results = 7
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View = 8
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Help = 9
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NewItem = 10
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FlowsheetSurfaceSelected = 11
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FlowsheetSurfaceNotSelected = 12
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ToolStrip = 13
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InitializationScript = 14
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End Enum
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Public Enum ExternalSolverCategory
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LinearSystem = 0
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NonLinearSystem = 1
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NonLinearMinimization = 2
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OrdinaryDifferentialEquations = 3
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End Enum
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Public Enum SpecCalcMode
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AfterSourceObject = 0
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BeforeTargetObject = 1
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BeforeFlowsheet = 2
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AfterFlowsheet = 3
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End Enum
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Public Enum SpecCalcMode2
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GlobalSetting = 0
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AfterSourceObject = 1
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BeforeTargetObject = 2
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BeforeFlowsheet = 3
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AfterFlowsheet = 4
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AfterObject = 5
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BeforeObject = 6
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End Enum
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Public Enum DimensionName
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NotDefined
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Length
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Diameter
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Height
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Area
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Volume
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Flow
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MassFlow
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Head
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Efficiency
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Power
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HeatDuty
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Pressure
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PressureDifference
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NumberOfTubes
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NumberofPackings
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NumberOfSections
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NumberOfTrays
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NumberOfCells
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End Enum
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End Namespace
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Namespace Enums.GraphicObjects
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Public Enum ConType
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ConIn = -1
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ConOut = 1
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ConEn = 0
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ConSp = 2
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End Enum
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Public Enum ConDir
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Up
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Down
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Right
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Left
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End Enum
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Public Enum ObjectType
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NodeIn
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NodeOut
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NodeEn
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Pump
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Tank
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Vessel
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MaterialStream
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EnergyStream
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Compressor
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Expander
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TPVessel
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Cooler
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Heater
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Pipe
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Valve
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Nenhum
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GO_Table
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GO_Text
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GO_Image
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GO_FloatingTable
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OT_Adjust
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OT_Spec
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OT_Recycle
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RCT_Conversion
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RCT_Equilibrium
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RCT_Gibbs
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RCT_CSTR
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RCT_PFR
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HeatExchanger
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ShortcutColumn
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DistillationColumn
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AbsorptionColumn
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RefluxedAbsorber
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ReboiledAbsorber
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OT_EnergyRecycle
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GO_Animation
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ComponentSeparator
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OrificePlate
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CustomUO
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ExcelUO
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CapeOpenUO
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FlowsheetUO
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GO_MasterTable
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SolidSeparator
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Filter
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GO_SpreadsheetTable
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GO_Rectangle
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CompressorExpander
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HeaterCooler
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GO_Chart
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GO_InputControl
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External
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AnalogGauge
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DigitalGauge
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LevelGauge
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Controller_PID
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Switch
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Input
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GO_HTMLText
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GO_Button
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AirCooler2
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WindTurbine
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HydroelectricTurbine
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SolarPanel
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PEMFuelCell
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WaterElectrolyzer
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RCT_GibbsReaktoro
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EnergyMixer
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Mixer
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Splitter
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Controller_Python
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Dummy
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SolidOps
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End Enum
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Public Enum ShapeIcon
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DefaultShape
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NodeIn
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NodeOut
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Pump
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Tank
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Vessel
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Compressor
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Expander
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Cooler
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Heater
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Pipe
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Valve
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RCT_Conversion
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RCT_Equilibrium
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RCT_Gibbs
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RCT_CSTR
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RCT_PFR
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HeatExchanger
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DistillationColumn
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AbsorptionColumn
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ComponentSeparator
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OrificePlate
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End Enum
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Public Enum Status
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Calculated
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Calculating
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ErrorCalculating
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Inactive
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Idle
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NotCalculated
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Modified
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End Enum
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Public Enum FontStyle
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Regular = 0
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Bold = 1
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Italic = 2
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BoldItalic = 3
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End Enum
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Public Enum PointValueType
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Temperature = 0
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Pressure = 1
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Flow = 2
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EnergyFlow = 3
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Concentration = 4
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CompoundMassFlow = 5
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CompoundMolarFlow = 6
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CompoundMassFraction = 7
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CompoundMolarFraction = 8
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MeanSolidParticleSize = 9
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End Enum
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End Namespace
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