modelHEXvle2vle_L3_2ph_BU_simple

VLE 2 VLE | L3 | 2 phase at shell side | Block shape | U-type | simple HT
Diagram of HEXvle2vle_L3_2ph_BU_simple

Extends from ClaRa.Basics.Icons.HEX04, ClaRa.Basics.Icons.ComplexityLevel (Displays the complexity level inside model icon ).

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
Real[2]yps_nom{yps_liq_nom, 1 - yps_liq_nom}Relative volume of liquid phase [1] and vapour phase [2] at nominal point
Shell Side › Fundamental Definitions
TILMedia.VLEFluid.Types.BaseVLEFluidmedium_shellsimCenter.fluid1Medium to be used for shell flow
General › Fundamental Definitions
BooleanuseHomotopysimCenter.useHomotopyTrue, if homotopy method is used during initialisation
Shell Side › Geometry
ClaRa.Basics.Units.Lengthlength10Length of the HEX
ClaRa.Basics.Units.Lengthheight3Height of HEX
ClaRa.Basics.Units.Lengthwidth3Width of HEX
ClaRa.Basics.Units.Lengthz_in_shellheightInlet position from bottom
ClaRa.Basics.Units.Lengthz_in_aux1heightInlet position of auxilliary1 from bottom
ClaRa.Basics.Units.Lengthz_in_aux2heightInlet position of auxilliary2 from bottom
ClaRa.Basics.Units.Lengthz_out_shell0.1Outlet position from bottom
ClaRa.Basics.Units.Lengthradius_flange0.05Flange radius of all flanges
ClaRa.Basics.Units.Massmass_struc0Mass of inner structure elements, additional to the tubes itself
ClaRa.Basics.Units.Lengthheight_hotwell1Height of the hotwell
ClaRa.Basics.Units.Lengthwidth_hotwell1Width of the hotwell
ClaRa.Basics.Units.Lengthlength_hotwell1Length of the hotwell
Shell Side › Nominal Values
ClaRa.Basics.Units.MassFlowRatem_flow_nom_shell10Nominal mass flow on shell side
ClaRa.Basics.Units.Pressurep_nom_shell10Nominal pressure on shell side
ClaRa.Basics.Units.EnthalpyMassSpecifich_nom_shell100e3Nominal specific enthalpy on shell side
Realyps_liq_nomlevel_rel_startRelative volume of liquid phase at nominal point
Shell Side › Initialisation
ClaRa.Basics.Units.EnthalpyMassSpecifich_liq_start-10 + TILMedia.VLEFluid.MixtureCompatible.Functions.bubbleSpecificEnthalpy_pxi(medium_shell, p_start_shell)Start value of liquid specific enthalpy
ClaRa.Basics.Units.EnthalpyMassSpecifich_vap_start+10 + TILMedia.VLEFluid.MixtureCompatible.Functions.dewSpecificEnthalpy_pxi(medium_shell, p_start_shell)Start value of vapour specific enthalpy
ClaRa.Basics.Units.Pressurep_start_shell1e5Start value of shell fluid pressure
Reallevel_rel_start0.5Start value for relative filling Level
IntegerinitOptionShell211Type of initialisation
Tubes › Fundamental Definitions
TILMedia.VLEFluid.Types.BaseVLEFluidmedium_tubessimCenter.fluid1Medium to be used for tubes flow
Tubes › Tubes Geometry
ClaRa.Basics.Units.Lengthdiameter_i0.048Inner diameter of internal tubes
ClaRa.Basics.Units.Lengthdiameter_o0.05Outer diameter of internal tubes
IntegerN_tubes1000Number of tubes
IntegerN_passes1Number of passes of the internal tubes
ClaRa.Basics.Units.Lengthz_in_tubeslength/2Inlet position from bottom
ClaRa.Basics.Units.Lengthz_out_tubeslength/2Outlet position from bottom
BooleanstaggeredAlignmenttrueTrue, if the tubes are aligned staggeredly
ClaRa.Basics.Units.LengthDelta_z_par1.5*diameter_oDistance between tubes parallel to flow direction (center to center)
ClaRa.Basics.Units.LengthDelta_z_ort1.5*diameter_oDistance between tubes orthogonal to flow direction (center to center)
IntegerN_rowsinteger(ceil(sqrt(N_tubes))*N_passes)Number of pipe rows in shell flow direction
RealCF_geo1Correction coefficient due to fins etc.
Tubes › Nominal Values
ClaRa.Basics.Units.MassFlowRatem_flow_nom_tubes10Nominal mass flow on tubes side
ClaRa.Basics.Units.Pressurep_nom_tubes10Nominal pressure on side tubes
ClaRa.Basics.Units.EnthalpyMassSpecifich_nom_tubes10Nominal specific enthalpy on tubes side
ClaRa.Basics.Units.HeatFlowRateQ_flow_nom1e6Nominal heat flow rate
Tubes › Initialisation
ClaRa.Basics.Units.EnthalpyMassSpecifich_start_tubes1e5Start value of tube fluid specific enthalpy
ClaRa.Basics.Units.Pressurep_start_tubes1e5Start value of tube fluid pressure
IntegerinitOptionTubes0Type of initialisation at tube side
Tube Wall › Initialisation
ClaRa.Basics.Units.Temperature[3]T_w_startones(3)*293.15Initial wall temperature inner --> outer
IntegerinitOptionWall213Init option of Tube wall
Expert Settings › Zone Interaction at Shell Side
ClaRa.Basics.Units.TimeTau_cond0.3Time constant of condensation
ClaRa.Basics.Units.TimeTau_evap0.03Time constant of evaporation
ClaRa.Basics.Units.CoefficientOfHeatTransferalpha_ph50000HTC of the phase border
ClaRa.Basics.Units.AreaA_phaseBordershell.geo.A_hor*100Heat transfer area at phase border
RealexpHT_phases0Exponent for volume dependency on inter phase HT
RealabsorbInflow1Absorption of incoming mass flow to the zones 1: perfect in the allocated zone, 0: perfect according to steam quality
BooleanequalPressurestrueTrue if pressure in liquid and vapour phase is equal
Expert Settings › Mass Accumulation at Shell Side
Modelica.Blocks.Types.SmoothnesssmoothnessModelica.Blocks.Types.Smoothness.LinearSegmentsSmoothness of level calculation (table based)
Summary and Visualisation
BooleanshowExpertSummarysimCenter.showExpertSummaryTrue, if expert summary should be applied
BooleanshowDatatrueTrue, if a data port containing p,T,h,s,m_flow shall be shown, else false
BooleanlevelOutputfalseTrue, if Real level connector shall be addded
BooleanoutputAbsfalseTrue, if absolute level is at output

Connectors

TypeNameDefaultDescription
ClaRa.Basics.Interfaces.FluidPortInIn2
ClaRa.Basics.Interfaces.FluidPortOutOut2
ClaRa.Basics.Interfaces.FluidPortOutOut1
ClaRa.Basics.Interfaces.FluidPortInIn1
ClaRa.Basics.Interfaces.EyeOuteye2
ClaRa.Basics.Interfaces.EyeOuteye1
ClaRa.Basics.Interfaces.FluidPortInaux1
ClaRa.Basics.Interfaces.FluidPortInaux2
Modelica.Blocks.Interfaces.RealOutputlevelif outputAbs then summary.outline.level_abs else summary.outline.level_rel

Components

TypeNameDefaultDescription
Stringcomplexity (from ComplexityLevel)"??"
ClaRa.SimCentersimCenter
ClaRa.Basics.ControlVolumes.FluidVolumes.VolumeVLE_L2tubes
ClaRa.Basics.ControlVolumes.FluidVolumes.VolumeVLE_L3_TwoZonesNPortshell
ClaRa.Basics.ControlVolumes.SolidVolumes.CylindricalThickWall_L4wall
Summarysummary

Contents

NameDescription
Outline
Summary
HeatTransfer_Shell
PressureLossShell
HeatTransferTubes
PressureLossTubes
WallMaterial

Revisions

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