modelVolumeVLE_L3_TwoZones

A volume element balancing liquid and vapour phase

Extends from ClaRa.Basics.Icons.Volume2Zones, ClaRa.Basics.Icons.ComplexityLevel (Displays the complexity level inside model icon ).

Information

Model description: A non-adiabatic control volume without friction losses taking the geostatic pressure difference into account

  • This model is derived from ThermoPower.Water.Header
  • Flow reversal is supported
  • Homotopy initialisation is supported

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
Modelica.Units.SI.Densityrho_liq_nomTILMedia.VLEFluid.MixtureCompatible.Functions.bubbleDensity_pxi(medium, p_nom)Nominal density
Modelica.Units.SI.Densityrho_vap_nomTILMedia.VLEFluid.MixtureCompatible.Functions.dewDensity_pxi(medium, p_nom)Nominal density
BooleanshowExpertSummaryfalse|Summary and Visualisation||True, if expert summary should be applied
Fundamental Definitions
TILMedia.VLEFluid.Types.BaseVLEFluidmediumsimCenter.fluid1Medium in the component
Phase Border
ClaRa.Basics.Units.TimeTau_cond10Time constant of condensation
ClaRa.Basics.Units.TimeTau_evapTau_cond/1000Time constant of evaporation
ClaRa.Basics.Units.CoefficientOfHeatTransferalpha_ph50000HTC of the phase border
ClaRa.Basics.Units.AreaA_heat_phgeo.A_hor*100Heat transfer area at phase border
RealexpHT_phases0Exponent for volume dependency on inter phase HT
BooleanequalPressurestrueTrue if pressure in liquid and vapour phase is equal
Initialisation
BooleanuseHomotopysimCenter.useHomotopyTrue, if homotopy method is used during initialisation
ClaRa.Basics.Units.EnthalpyMassSpecifich_liq_start-10 + TILMedia.VLEFluid.MixtureCompatible.Functions.bubbleSpecificEnthalpy_pxi(medium, p_start)Start value of sytsem specific enthalpy
ClaRa.Basics.Units.EnthalpyMassSpecifich_vap_start+10 + TILMedia.VLEFluid.MixtureCompatible.Functions.dewSpecificEnthalpy_pxi(medium, p_start)Start value of sytsem specific enthalpy
Modelica.Units.SI.Pressurep_start1e5Start value of sytsem pressure
Reallevel_rel_start0.5Start value for relative filling level
IntegerinitOption0Type of initialisation
General › Nominal Values
Modelica.Units.SI.MassFlowRatem_flow_nom10Nominal mass flow rates at inlet
Nominal Values
Modelica.Units.SI.Pressurep_nom1e5Nominal pressure
Geometry
IntegerheatSurfaceAlloc1Heat transfer area to be considered

Connectors

TypeNameDefaultDescription
ClaRa.Basics.Interfaces.FluidPortIninletInlet port
ClaRa.Basics.Interfaces.FluidPortOutoutletOutlet port
ClaRa.Basics.Interfaces.HeatPort_aheat

Components

TypeNameDefaultDescription
Stringcomplexity (from ComplexityLevel)"??"
ClaRa.SimCentersimCenter
ClaRa.Basics.Units.EnthalpyMassSpecifich_liqSpecific enthalpy of liquid phase
ClaRa.Basics.Units.EnthalpyMassSpecifich_vapSpecific enthalpy of vapour phase
Realdrho_liqdt
Realdrho_vapdt
ClaRa.Basics.Units.Volumevolume_liqLiquid volume
ClaRa.Basics.Units.Volumevolume_vapVapour volume
Real[2]yps{phaseBorder.level_rel, 1 - phaseBorder.level_rel}Relative volume of liquid phase [1] and vapour phase [2]
ClaRa.Basics.Units.MassFlowRatem_flow_condCondensing mass flow
ClaRa.Basics.Units.MassFlowRatem_flow_evapEvaporating mass flow
ClaRa.Basics.Units.HeatFlowRateQ_flow_phasesHeat flow between phases
ClaRa.Basics.Units.Massmass_liqLiquid mass
ClaRa.Basics.Units.Massmass_vapVapour mass
ClaRa.Basics.Units.Pressurep_liqLiquid pressure
ClaRa.Basics.Units.Pressurep_vapVapour pressure
ClaRa.Basics.Units.EnthalpyFlowRateH_flow_inliqEnthalpy flow rate passing from inlet to liquid zone and vice versa
ClaRa.Basics.Units.EnthalpyFlowRateH_flow_invapEnthalpy flow rate passing from inlet to vapour zone and vice versa
ClaRa.Basics.Units.EnthalpyFlowRateH_flow_outliqEnthalpy flow rate passing from inlet to liquid zone and vice versa
ClaRa.Basics.Units.EnthalpyFlowRateH_flow_outvapEnthalpy flow rate passing from outlet to vapour zone and vice versa
TILMedia.VLEFluid.MixtureCompatible.VLEFluid_phfluidIn
TILMedia.VLEFluid.MixtureCompatible.VLEFluid_phfluidOut
HeatTransferheattransfer
Geometrygeo
PhaseBorderphaseBorder
PressureLosspressureLoss
Summarysummary

Contents

NameDescription
Outline
Summary
HeatTransfer
PhaseBorder
PressureLoss
Geometry

Revisions

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