modelBend

Bend
Diagram of Bend

Information

## Copyright © EDF 2002 - 2026   
## ThermoSysPro Version 4.2   
This component model is documented in Sect. 13.6 of the ThermoSysPro book.

Parameters

TypeNameDefaultDescription
Units.SI.DiameterD0.2Pipe diameter
Units.SI.RadiusR00.2Pipe radius
ThermoSysPro.Units.nonSI.Angle_degdelta90Pipe angle
Realrugosrel0Pipe roughness
BooleanK_A1_Tabuletruetrue: A1 is computed using linear interpolation - false: A1 is computed using correlation formula
BooleanK_B1_Tabuletruetrue: B1 is computed using linear interpolation - false: B1 is computed using correlation formula
Units.SI.MassFlowRategamma_diff1e-4Diffusion conductance (active if diffusion=true in neighbouring volumes)
Fluid › Fluid properties
Units.SI.Densityp_rho0If > 0, fixed fluid density
IF97RegionregionIF97Region.All_regionsIF97 region (active for IF97 water/steam only)

Connectors

TypeNameDefaultDescription
ThermoSysPro.Fluid.Interfaces.Connectors.FluidInletC1
ThermoSysPro.Fluid.Interfaces.Connectors.FluidOutletC2

Components

TypeNameDefaultDescription
RealkhiHydraulic pressure loss coefficient
RealkhimSingular pressure loss coefficient
RealkhifFriction pressure loss coefficient
RealkdeltaRoughness factor for the singular pressure loss
ThermoSysPro.Units.SI.PressureDifferencedeltaPPresure loss
Units.SI.MassFlowRateQMass flow rate
Units.SI.ReynoldsNumberReReynolds number
Units.SI.ReynoldsNumberRelimLimit Reynolds number
RealyA1Output of table A1
RealyB1Output of table B1
RealyC1Output of table C1
ReallambdaFriction pressure loss coefficient
Units.SI.DensityrhoFluid density
Units.SI.DynamicViscositymuFluid dynamic viscosity
Units.SI.TemperatureTFluid temperature
Units.SI.AbsolutePressurePmFluid average pressure
Units.SI.SpecificEnthalpyhFluid specific enthalpy
FluidTypeftypeFluid type
IntegerfluidInteger(ftype)Fluid number
ThermoSysPro.InstrumentationAndControl.Blocks.Tables.Table1DTA1
ThermoSysPro.InstrumentationAndControl.Blocks.Tables.Table1DTB1

Revisions

Authors  

Daniel Bouskela  
Baligh El Hefni