modelNusseltPipe1ph_L2

Pipe Geo || L2 || HTC || Nusselt || 1ph

Extends from ClaRa.Basics.ControlVolumes.Fundamentals.HeatTransport.VLE_HT.HeatTransfer_L2 ( L2 || HT-BaseClass), ClaRa.Basics.ControlVolumes.Fundamentals.HeatTransport.TubeTypeVLE_L2 (Partial heat transfer model for tube-type models).

Information

For detailed model documentation please consult the html-documentation shipped with ClaRa.

 


Authorship and Copyright Statement for original (initial) Contribution

Author:

DYNCAP/DYNSTART development team, Copyright © 2011-2024.

References:

For references please consult the html-documentation shipped with ClaRa.

Remarks:

This component was developed by ClaRa development team under the 3-clause BSD License.

Acknowledgements:

ClaRa originated from the collaborative research projects DYNCAP and DYNSTART. Both research projects were supported by the German Federal Ministry for Economic Affairs and Energy (FKZ 03ET2009 and FKZ 03ET7060).

CLA:

The author(s) have agreed to ClaRa CLA, version 1.0. See https://claralib.com/pdf/CLA.pdf

By agreeing to ClaRa CLA, version 1.0 the author has granted the ClaRa development team a permanent right to use and modify his initial contribution as well as to publish it or its modified versions under the 3-clause BSD License.

The ClaRa development team consists of the following partners:

TLK-Thermo GmbH (Braunschweig, Germany)

XRG Simulation GmbH (Hamburg, Germany).

Parameters

TypeNameDefaultDescription
Stringvle (from HeatTransferBaseVLE)"true"
BooleanuseHomotopy (from HeatTransfer_L2)
Stringtube (from TubeTypeVLE_L2)"true"
Integerboundary1Choice of heat transfer boundary condition, relevant for laminar flow heat transfer
Integercorrelation2Cprrelation type
RealCF_alpha_tubes1Correction factor due to fouling
IntegerheatSurfaceAlloc1To be considered heat transfer area
ClaRa.Basics.Units.CoefficientOfHeatTransferalpha_nomCF_alpha_tubes*(sm(laminar, turbulent, Re_nom)*alpha_lam_nom + sm(turbulent, laminar, Re_nom)*alpha_turb_nom)Nominal HTC (used for homotopy)
ClaRa.Basics.Units.ThermalResistanceHR_nom1/(alpha_nom*geo.A_heat_CF[heatSurfaceAlloc])Nominal convective heat resistance
Heat Transfer
StringtemperatureDifference (from HeatTransfer_L2)"Logarithmic mean - smoothed"Temperature Difference

Connectors

TypeNameDefaultDescription
ClaRa.Basics.Interfaces.HeatPort_aheat (from HeatTransfer_L2)

Components

TypeNameDefaultDescription
ClaRa.Basics.Records.IComVLE_L2iCom (from HeatTransfer_L2)
Units.TemperatureDelta_T_wi (from HeatTransfer_L2)Temperature difference between wall and fluid inlet temperature
Units.TemperatureDelta_T_wo (from HeatTransfer_L2)Temperature difference between wall and fluid outlet temperature
Units.TemperatureDelta_T_mean (from HeatTransfer_L2)Mean temperature difference used for heat transfer calculation
Units.TemperatureDelta_T_U (from HeatTransfer_L2)Upper temperature difference
Units.TemperatureDelta_T_L (from HeatTransfer_L2)Lower temperature difference
ClaRa.SimCentersimCenter
ClaRa.Basics.ControlVolumes.Fundamentals.Geometry.PipeGeometrygeo
ClaRa.Basics.Units.CoefficientOfHeatTransferalphaHeat transfer coefficient used for heat transfer calculation
ClaRa.Basics.Units.CoefficientOfHeatTransferalpha_lamHeat transfer coefficient - laminar part
ClaRa.Basics.Units.CoefficientOfHeatTransferalpha_turbHeat transfer coefficient - turbolent part
ClaRa.Basics.Units.ThermalResistanceHRConvective heat resistance
RealfailureStatus0== boundary conditions fulfilled | 1== failure >> check if still meaningfull results
ClaRa.Basics.Units.MassFlowRatem_flowMass flow rate
ClaRa.Basics.Units.VelocityvelocityMean velocity
ClaRa.Basics.Units.ReynoldsNumberReReynolds number
ClaRa.Basics.Units.PrandtlNumberPrPrandtl number

Revisions

For revisions please consult the html-documentation shipped with ClaRa.