# Enumerated Types

Enumerated Types
Type | Values
3WayValveDuty | 1 = Mixing (all ports open) 2 = Diverting (2 ports open)
AccumulatorRDRatio | 0 = 0 1 = 0.02 2 = 0.04 3 = 0.06 4 = 0.1 5 = >0.15
CompressorHeatTransfer | 0 = Ignore Heat Loss/Gain 1 = Fixed Temperature Change 2 = Fixed Transfer Rate 4 = Adiabatic Compression
ControllerMeasurementLocation | 0 = Upstream 1 = Downstream
ControllerMeasurementType | 0 = Stagnation Pressure 1 = Static Pressure
CrossBranchAngles | 90 = 90°
CrossJunctionType | 0 = Idelchik
CycloneEquation | 0 = Basic Principles 1 = Miller and Lissman 2 = Shepherd and Lapple 3 = Casal and Martinez-Benet
CycloneInletGeometry | 0 = Cylindrical 1 = Rectangular/Square
ElementTextAlignment | 0 = Top 1 = Bottom 2 = Left 3 = Right
ExchangerFluidSide | 0 = Tubeside 1 = Shellside
ExchangerPitchType | 0 = In-Line 1 = Staggered
ExpansionJointType | 0 = Lyre Bend 1 = II Shaped Bend 2 = Stuffing Box
FlashTypeCalculation | 0 = Isenthalpic Flash
FlowDirection | 1 = Out of Network -1 = Into Network
FlowScaleFactorType | 0 = None 1 = Fixed Value
FluidTypeNN | 1 = Newtonian/NN-NonSettling 4 = Heterogeneous Settling 14 = Pulp/Paper Stock
FluidTypeTwoPhase | 1 = Newtonian 9 = Two Phase
FluidTypeTwoPhaseNN | 1 = Newtonian/NN-NonSettling 4 = Heterogeneous Settling 9 = Two Phase 14 = Pulp/Paper Stock
FrictionModel | 0 = Moody 1 = Hazen Williams 2 = Fixed Friction Factor
Geometry | 0 = Cylindrical 1 = Rectangular/Square 2 = Annulus
HeatExchangerLossModel | 0 = Standard Relationships 1 = Manufacturer Loss Data 2 = Fixed Value
HeatLossModel | 0 = Ignore Heat Loss/Gain 1 = Fixed Temperature Change 2 = Fixed Transfer Rate 3 = Do Heat Transfer Calculation
HeatTransferModel | 0 = Ignore Heat Loss/Gain 1 = Fixed Temperature Change 2 = Fixed Transfer Rate
HideShow | 0 = Hide 1 = Show
IdelchikTeeAngles | 90 = 90° 60 = 60° 45 = 45° 30 = 30° 15 = 15°
JunctionConstruction | 0 = Welded, Flanged or Smooth 1 = Screwed or Sharp Edged
KLossBasis | 0 = Upstream Velocity 1 = Downstream Velocity
KOPotPressureModel | 0 = Auto Calculate 1 = Fixed Pressure
MillerTeeAngles | 90 = 90° 45 = 45°
MitreType | 1 = Miller 3 = Crane
NNSolidsPercent | 0 = Cw Weight % 1 = Cv Volume %
NozzleEqn | 0 = ISO 5157 Nozzle 1 = Long Radius Nozzle
OrificeEqn | 0 = ISO 5167
OrificeSelectionCriteria | 0 = Size for Flow 1 = Size for Pressure Loss
PhaseState | 0 = Undefined 1 = Liquid 2 = Saturated Liquid 3 = Gas or Vapor 4 = Slurry 5 = Solid/Gas 6 = Non-Newtonian 7 = Solid 8 = 2 Phase Frozen Liquid Vapor 9 = 2 Phase Single Liquid Vapor 10 = 2 phase Multicomponent Liquid Vapor 11 = Forced Liquid 12 = Forced Gas or Vapor 13 = Forced 2 Phase 14 = Pulp Paper Stock
PipeOutlet | 0 = Ignore Entry/Exit Loss 1 = Flush Sharp Edged 2 = Flush Bellmouth 3 = Inward Projecting
PressureControllerType | 0 = Pressure Sustaining 1 = Pressure Reducing
PulpPaperModel | 0 = Moller 1 = TAPPI (TIP 0310-12)
PumpSelectionCriteria | 0 = Size for Flow 1 = Size for Pressure Rise
ReducerType | 0 = Concentric 1 = Eccentric
ReliefValveOrificeSize | 0 = D - 0.11in2 / 71mm2 1 = E - 0.196in2 / 127mm2 2 = F - 0.307in2 / 198mm2 3 = G - 0.503in2 / 325mm2 4 = H - 0.785in2 / 506mm2 5 = J - 1.287in2 / 830mm2 6 = K - 1.838in2 / 1185mm2 7 = L - 2.853in2 / 1840mm2 8 = M - 3.60in2 / 2320mm2 9 = N - 4.34in2 / 2800mm2 10 = P - 6.38in2 / 4120mm2 11 = Q - 11.05in2 / 7130mm2 12 = R - 16.0in2 / 10300mm2 13 = T - 26.0in2 / 16770mm2
SafetyReliefValveModel | 0 = Internal 1 = Iso 4162
SlurryFlowBasis | 0 = Total Slurry Flow 1 = Solids Only 2 = Carrier Only
SlurryPumpDerating | 0 = None 1 = Fixed Reduction Ratio 2 = King 3 = HI Guidelines
TeeJunctionType | 0 = Idelchik 1 = Miller 3 = Crane 4 = SAE
TwoPhaseFlowBasis | 0 = Total Flow 1 = Liquid Only 2 = Gas Only
UserDefinedEquation | 0 = §P = K + ABQ^n + CDQ^m
UserDefinedTermType | 0 = Fixed Value 1 = Inlet Density 2 = Inlet Viscosity 3 = Inlet Pressure
VenturiTubeType | 0 = Welded 1 = Cast 2 = Machined
VesselType | 0 = Cylindrical Flat Bottom 1 = Rectangular Flat Bottom
WyeJunctionType | 0 = Idelchik 4 = SAE