modelPlateHEXvle2vle_L3_2ph_ntu

VLE 2 VLE | L2 | PlateHEX NTU
Diagram of PlateHEXvle2vle_L3_2ph_ntu

Extends from ClaRa.Basics.Icons.HEX01Plate.

Information

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

 


Authorship and Copyright Statement for original (initial) Contribution

Author:

ClaRa development team, Copyright © 2017 - 2022.

References:

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

Remarks:

This component was developed for ClaRa library.

Acknowledgements:

CLA:

Parameters

TypeNameDefaultDescription
BooleanshowExpertSummarysimCenter.showExpertSummary|Summary and Visualisation||True, if expert summary should be applied
BooleanshowDatatrue|Summary and Visualisation||True, if a data port containing p,T,h,s,m_flow shall be shown, else false
General › Fundamental Definitions
TILMedia.VLEFluid.Types.BaseVLEFluidmedium_asimCenter.fluid1Medium to be used for flow 1
TILMedia.VLEFluid.Types.BaseVLEFluidmedium_bsimCenter.fluid1Medium to be used for flow 2
General › Geometry
ClaRa.Basics.Units.Lengthwidth1Plate width
ClaRa.Basics.Units.Lengthlength1Plate length
ClaRa.Basics.Units.Lengththickness_wall0.01Wall thickness of the plate
IntegerN_plates4Number of tubes in parallel
ClaRa.Basics.Units.Lengthamp0.001Amplitude of corrugated plate
ClaRa.Basics.Units.Lengthlength_wave2*Modelica.Constants.pi*ampWave length of corrugated plate
ClaRa.Basics.Units.Anglephi60*Modelica.Constants.pi/180Corrugation angle
ClaRa.Basics.Units.Lengthz_in_alength/2Inlet position from bottom for flow_a
ClaRa.Basics.Units.Lengthz_out_alength/2Outlet position from bottom for flow_a
ClaRa.Basics.Units.Lengthz_in_blength/2Inlet position from bottom for flow_b
ClaRa.Basics.Units.Lengthz_out_blength/2Outlet position from bottom for flow_b
Real[2]CF_geoones(2)Correction factor for heat transfer area dedicated to surfuca of: 1|flow_a 2|flow_b
Flow_a › Fundamental Definitions
BooleanfrictionAtInlet_afalseTrue if pressure loss between first cell and inlet shall be considered
BooleanfrictionAtOutlet_afalseTrue if pressure loss between last cell and outlet shall be considered
Flow_a › Nominal Values Flow_a
SI.MassFlowRatem_nom_a1Nominal mass flow on A side
SI.Pressurep_nom_a1e5Nominal pressure on A side
SI.EnthalpyMassSpecifich_nom_a85e3Nominal specific enthalpy on A side
SI.PressureDelta_p_nom_a1000Nominal pressure loss on A side
Flow_b › Nominal Values Flow_b
SI.MassFlowRatem_nom_b1Nominal mass flow on tube side
SI.Pressurep_nom_b1e5Nominal pressure on tube side
SI.EnthalpyMassSpecifich_nom_b85e3Nominal specific enthalpy on tube side
SI.PressureDelta_p_nom_b1000Nominal pressure loss on tube side
Flow_b › Fundamental Definitions
BooleanfrictionAtInlet_bfalseTrue if pressure loss between first cell and inlet shall be considered
BooleanfrictionAtOutlet_bfalseTrue if pressure loss between last cell and outlet shall be considered
Wall › Fundamental Definitions
SI.Massmass_struc0Additional to mass of the plate HX calculated by density*length*width*thicknesswall
Initialisation
BooleanuseHomotopysimCenter.useHomotopytrue, if homotopy method is used during initialisation
Initialisation › Flow_a
IntegerinitOption_a0Type of initialisation
SI.EnthalpyMassSpecifich_start_a85e3Start value of sytsem specific enthalpy
SI.Pressurep_start_a1e5Start value of sytsem pressure
SI.MassFraction[medium_a.nc - 1]xi_start_azeros(medium_a.nc - 1)Initial composition for flow_a
Initialisation › Flow_b
IntegerinitOption_b0Type of initialisation
SI.EnthalpyMassSpecifich_start_b85e3Start value of sytsem specific enthalpy
SI.Pressurep_start_b1e5Start value of sytsem pressure
SI.MassFraction[medium_b.nc - 1]xi_start_bzeros(medium_b.nc - 1)Initial composition for flow_b
Initialisation › Wall
IntegerinitOptionWall0|Initialisation option for wall
SI.Temperature[3]T_w_a_startones(3)*293.15Initial wall temperature flow_a side
SI.Temperature[3]T_w_b_startones(3)*293.15Initial wall temperature flow_b side
IntegerinitOption_yps3Volumetric initialisation
Real[2]yps_start{0.33, 0.33}Initial area fraction 1phase | 2phase
Expert Settings › NTU model
Realgain_eff1Avoid effectiveness > 1, high gain_eff leads to stricter observation but may cause numeric errors
ClaRa.Basics.Units.TimeTau_stab0.1Time constant for numeric stabilisation w.r.t. heat flow rates

Connectors

TypeNameDefaultDescription
ClaRa.Basics.Interfaces.FluidPortInIn_b
ClaRa.Basics.Interfaces.FluidPortOutOut_b
ClaRa.Basics.Interfaces.FluidPortOutOut_a
ClaRa.Basics.Interfaces.FluidPortInIn_a
ClaRa.Basics.Interfaces.EyeOuteye2
ClaRa.Basics.Interfaces.EyeOuteye1

Components

TypeNameDefaultDescription
ClaRa.SimCentersimCenter
ClaRa.Basics.ControlVolumes.FluidVolumes.VolumeVLE_L2flow_a
ClaRa.Basics.ControlVolumes.FluidVolumes.VolumeVLE_L2flow_b
ClaRa.Basics.ControlVolumes.SolidVolumes.NTU_plate_L3_standalonethinWall
Summarysummary

Contents

NameDescription
Outline
Summary
HeatExchangerType
HeatTransferInner_a
PressureLoss_a
HeatTransferInner_b
PressureLoss_b
WallMaterial
HeatCapacityAveraging

Revisions

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