modelPartialHeatTransfer_setT

Base model
Diagram of PartialHeatTransfer_setTOpen the diagram

Parameters

TypeNameDefaultDescription
Internal Interface
RealnParallel1Number of parallel components
IntegernHT1Number of heat transfer segments
IntegernSurfaces1Number of heat transfer surfaces
IntegerflagIdeal0Flag for models to handle ideal boundary
Internal Interface › Initialization
SI.Temperature[nHT]Ts_start
Advanced
SI.ReynoldsNumberRe_lam2300Laminar transition Reynolds number
SI.ReynoldsNumberRe_turb4000Turbulent transition Reynolds number
Units.NonDimCF1.0Correction Factor: Q = CF*alpha*A*dT
Units.NonDim[nHT,nSurfaces]CFsfill(CF, nHT, nSurfaces)if non-uniform then set

Connectors

TypeNameDefaultDescription
HeatAndMassTransfer.Interfaces.HeatPort_Flow[nHT,nSurfaces]heatPorts

Components

TypeNameDefaultDescription
Medium.ThermodynamicState[nHT]statesThermodynamic state of fluid
SI.Velocity[nHT]vsFluid Velocity
SI.Diameter[nHT]dimensionsCharacteristic dimension (e.g. hydraulic diameter)
SI.Area[nHT]crossAreasCross sectional flow area
SI.Length[nHT]dlengthsCharacteristic length of heat transfer segment
SI.Height[nHT]roughnessesAverage height of surface asperities
SI.Area[nHT,nSurfaces]surfaceAreasSurface area for heat transfer
SI.Temperature[nHT]Ts_fluidMedium.temperature(states)Fluid temperature
SI.Temperature[nHT,nSurfaces]Ts_wallheatPorts.TWall temperature
SI.MassFlowRate[nHT]m_flowsFluid mass flow rate
SI.ReynoldsNumber[nHT]ResReynolds number
SI.PrandtlNumber[nHT]PrsPrandtl number
SI.CoefficientOfHeatTransfer[nHT,nSurfaces]alphasCoefficient of heat transfer
SI.NusseltNumber[nHT,nSurfaces]NusNusselt number
SI.HeatFlowRate[nHT,nSurfaces]Q_flowsheatPorts.Q_flow/nParallelHeat flow rate

Contents

NameDescription
Medium