modelTwoPhaseVarState

phases balanced seperately, states optional

Extends from ThermalSeparation.BalanceEquations.Base.NonEquilibrium.BaseTwoPhaseVarState (phases balanced seperately, states optional), ThermalSeparation.BalanceEquations.StructuredPackedColumn.BaseStructured.

Parameters

Type	Name	Default	Description
Integer	n (from BaseBalanceEquationsNonEq)		packed column: number of discrete elements in the section; plate column: number of trays in one section
Integer	nS (from BaseBalanceEquationsNonEq)		number of species which are equal in vapour and liquid phase
Integer	nSL (from BaseBalanceEquationsNonEq)	MediumLiquid.nSubstance
Integer	nSV (from BaseBalanceEquationsNonEq)	MediumVapour.nSubstance
Integer[nS,2]	mapping (from BaseBalanceEquationsNonEq)	{{i, i} for i in 1:nS}	parameter to map the different medium vectors one to another
Boolean[nSV]	inertVapour (from BaseBalanceEquationsNonEq)	fill(false, nSV)	true for each component which is inert in the vapour phase
Boolean[nSL]	inertLiquid (from BaseBalanceEquationsNonEq)	fill(false, nSL)	true for each component which is inert in the liquid phase
Modelica.Units.SI.Temperature	T_ref (from BaseBalanceEquationsNonEq)
Boolean	StartUp_CCS (from BaseBalanceEquationsNonEq)	falseannotation(Dialog(tab = "Propagated from Column", group = "These variables are propagated from the column model and do not have to be set by the user!", enable = false))
SI.Area	A (from BaseBalanceEquationsNonEq)		cross sectional area of the column
SI.Length	H (from BaseBalanceEquationsNonEq)		height of this section of the column
Real	eps (from BaseBalanceEquationsNonEq)		void fraction in the column
SI.Density[n]	rho_solid (from BaseBalanceEquationsNonEq)
SI.SpecificHeatCapacity	c_solid (from BaseBalanceEquationsNonEq)
Boolean	EQ	filmModel.EQ
Propagated from Column › These variables are propagated from the column model and do not have to be set by the user!
SI.Time	delay_startUp (from BaseBalanceEquationsNonEq)	200
Boolean	smooth_startUp (from BaseBalanceEquationsNonEq)	false
Boolean[nSV]	lowBoilingPoint (from BaseBalanceEquationsNonEq)	fill(false, nSV)
StartUp
Boolean	considerStartUp (from BaseBalanceEquationsNonEq)	false	true if StartUp is to be considered

Components

Type	Name	Default	Description
MediumVapour.BaseProperties[n]	mediumVapourStar (from BaseBalanceEquationsNonEq)
MediumLiquid.BaseProperties[n]	mediumLiquidStar (from BaseBalanceEquationsNonEq)
SI.Temperature[n]	T_star (from BaseBalanceEquationsNonEq)
SI.MoleFraction[n,nSL]	x_l_star (from BaseBalanceEquationsNonEq)
SI.MoleFraction[n,nSL]	c_l_star (from BaseBalanceEquationsNonEq)
SI.MoleFraction[n,nSV]	x_v_star (from BaseBalanceEquationsNonEq)
SI.MoleFraction[n,nSV]	c_v_star (from BaseBalanceEquationsNonEq)
SI.MoleFraction[n]	h_vap_star (from BaseBalanceEquationsNonEq)
SI.MoleFraction[n]	h_liq_star (from BaseBalanceEquationsNonEq)
MediumVapour.ThermodynamicProperties	propsVap (from BaseBalanceEquationsNonEq)
MediumVapour.ThermodynamicProperties	propsVapIn (from BaseBalanceEquationsNonEq)
MediumVapour.ThermodynamicState	stateVap (from BaseBalanceEquationsNonEq)
SI.Pressure[n,nSL]	p_sat (from BaseBalanceEquationsNonEq)
SI.Density[n]	rho_v (from BaseBalanceEquationsNonEq)	propsVap.d	mixture vapour density
SI.Density	rho_v_in (from BaseBalanceEquationsNonEq)	propsVapIn.d
SI.MolarMass[n]	MM_v (from BaseBalanceEquationsNonEq)	propsVap.MM	molar mass of the vapour mixture
SI.MolarMass	MM_v_in (from BaseBalanceEquationsNonEq)	propsVapIn.MM
SI.MolarMass[n]	MM_v_star (from BaseBalanceEquationsNonEq)	mediumVapourStar.MM
ThermalSeparation.Units.MolarEnthalpy[n]	h_v (from BaseBalanceEquationsNonEq)	propsVap.h
ThermalSeparation.Units.MolarEnthalpy	h_v_in (from BaseBalanceEquationsNonEq)	propsVapIn.h
SI.Pressure[n + 1]	p_v (from BaseBalanceEquationsNonEq)
SI.Pressure[n,nSL]	p_sat_bulk (from BaseBalanceEquationsNonEq)
MediumLiquid.ThermodynamicProperties	propsLiq (from BaseBalanceEquationsNonEq)
MediumLiquid.ThermodynamicProperties	propsLiqIn (from BaseBalanceEquationsNonEq)
MediumLiquid.ThermodynamicState	stateLiq (from BaseBalanceEquationsNonEq)
SI.Density[n]	rho_l (from BaseBalanceEquationsNonEq)	propsLiq.d	mixture liquid density
SI.Density	rho_l_in (from BaseBalanceEquationsNonEq)	propsLiqIn.d
SI.MolarMass[n]	MM_l (from BaseBalanceEquationsNonEq)	propsLiq.MM	molar mass of the liquid mixture
SI.MolarMass	MM_l_in (from BaseBalanceEquationsNonEq)	propsLiqIn.MM
ThermalSeparation.Units.MolarEnthalpy[n]	h_l (from BaseBalanceEquationsNonEq)	propsLiq.h
ThermalSeparation.Units.MolarEnthalpy	h_l_in (from BaseBalanceEquationsNonEq)	propsLiqIn.h
SI.Concentration[n,nSV]	c_v (from BaseBalanceEquationsNonEq)
SI.Concentration[nSV]	c_v_in (from BaseBalanceEquationsNonEq)	propsVapIn.c
SI.MoleFraction[nSV]	x_v_in (from BaseBalanceEquationsNonEq)	propsVapIn.x
SI.MoleFraction[n,nSV]	x_v (from BaseBalanceEquationsNonEq)
SI.VolumeFlowRate	Vdot_v_in (from BaseBalanceEquationsNonEq)
SI.VolumeFlowRate[n]	Vdot_v (from BaseBalanceEquationsNonEq)
SI.MoleFraction[nSV]	x_upStreamIn_act (from BaseBalanceEquationsNonEq)
SI.MoleFraction[nSV]	x_upStreamOut_act (from BaseBalanceEquationsNonEq)
ThermalSeparation.Units.MolarEnthalpy	h_upStreamIn_act (from BaseBalanceEquationsNonEq)
ThermalSeparation.Units.MolarEnthalpy	h_upStreamOut_act (from BaseBalanceEquationsNonEq)
SI.MoleFraction[n,nS]	x_vap_liq (from BaseBalanceEquationsNonEq)
SI.Concentration[n,nSL]	c_l (from BaseBalanceEquationsNonEq)
SI.Concentration[nSL]	c_l_in (from BaseBalanceEquationsNonEq)	propsLiqIn.c	molar concentration in the liquid at the liquid outlet of each stage
SI.MoleFraction[nSL]	x_l_in (from BaseBalanceEquationsNonEq)	propsLiqIn.x
SI.MoleFraction[n,nSL]	x_l (from BaseBalanceEquationsNonEq)	propsLiq.x
SI.VolumeFlowRate	Vdot_l_in (from BaseBalanceEquationsNonEq)
SI.VolumeFlowRate[n]	Vdot_l (from BaseBalanceEquationsNonEq)
SI.MoleFraction[nSL]	x_downStreamIn_act (from BaseBalanceEquationsNonEq)
SI.MoleFraction[nSL]	x_downStreamOut_act (from BaseBalanceEquationsNonEq)
ThermalSeparation.Units.MolarEnthalpy	h_downStreamIn_act (from BaseBalanceEquationsNonEq)
ThermalSeparation.Units.MolarEnthalpy	h_downStreamOut_act (from BaseBalanceEquationsNonEq)
SI.VolumeFlowRate[n]	Vdot_v_feed (from BaseBalanceEquationsNonEq)
SI.Concentration[n,nSV]	c_v_feed (from BaseBalanceEquationsNonEq)
SI.SpecificEnthalpy[n]	h_v_feed (from BaseBalanceEquationsNonEq)
SI.VolumeFlowRate[n]	Vdot_l_feed (from BaseBalanceEquationsNonEq)
SI.Concentration[n,nSL]	c_l_feed (from BaseBalanceEquationsNonEq)
SI.SpecificEnthalpy[n]	h_l_feed (from BaseBalanceEquationsNonEq)
SI.Density[n]	rho_l_feed (from BaseBalanceEquationsNonEq)
SI.Density[n]	rho_v_feed (from BaseBalanceEquationsNonEq)
SI.MolarMass[n]	MM_l_feed (from BaseBalanceEquationsNonEq)
SI.MolarMass[n]	MM_v_feed (from BaseBalanceEquationsNonEq)
SI.MolarFlowRate[n,nSV]	Ndot_v_transfer (from BaseBalanceEquationsNonEq)
SI.MolarFlowRate[n,nSL]	Ndot_l_transfer (from BaseBalanceEquationsNonEq)
SI.HeatFlowRate[n]	Edot_l_transfer (from BaseBalanceEquationsNonEq)
SI.HeatFlowRate[n]	Edot_v_transfer (from BaseBalanceEquationsNonEq)
SI.MolarFlowRate[n,nSL]	Ndot_reac (from BaseBalanceEquationsNonEq)
SI.HeatFlowRate[n]	Qdot_reac (from BaseBalanceEquationsNonEq)
Boolean[n]	bool_eps (from BaseBalanceEquationsNonEq)
SI.Temperature[n]	T (from BaseBalanceEquationsNonEq)	propsLiq.T
ThermalSeparation.Units.MolarEnthalpy[n,nSV]	delta_hv (from BaseBalanceEquationsNonEq)
SI.HeatFlowRate[n]	Qdot_wall (from BaseBalanceEquationsNonEq)		heat flow rate to wall
SI.MolarFlowRate[n]	Ndot_v (from BaseBalanceEquationsNonEq)		total molar flow rate vapour
SI.MolarFlowRate	Ndot_v_in (from BaseBalanceEquationsNonEq)		total molar flow rate vapour
SI.MolarFlowRate[n]	Ndot_l (from BaseBalanceEquationsNonEq)		total molar flow rate liquid
SI.MolarFlowRate	Ndot_l_in (from BaseBalanceEquationsNonEq)		total molar flow rate vapour
SI.VolumeFraction[n]	eps_liq (from BaseBalanceEquationsNonEq)		liquid volume fraction
SI.VolumeFraction[n]	eps_vap (from BaseBalanceEquationsNonEq)		vapour volume fraction
SI.VolumeFlowRate[n]	Vdot_le (from BaseBalanceEquationsNonEq)		liquid volume flow entrained by vapour
Real[n]	Ndot_source_startUp (from BaseBalanceEquationsNonEq)		dummy molar flow rate to account for discharge of inert gas during startUp
Boolean[n]	before_transition (from BaseBalanceEquationsNonEq)
Real	k (from BaseBalanceEquationsNonEq)
Real[n,nSL]	gamma (from BaseBalanceEquationsNonEq)
SI.Pressure[n + 1]	p_hyd (from BaseBalanceEquationsNonEq)		hydraulic pressure
Real[n]	omega (from BaseBalanceEquationsNonEq)
Boolean[n]	startUp (from BaseBalanceEquationsNonEq)
Boolean	stat (from BaseBalanceEquationsNonEq)		true for steady state balancing equations
SI.MolarInternalEnergy[n]	u_v (from BaseTwoPhaseVarState)
SI.MolarInternalEnergy[n]	u_l (from BaseTwoPhaseVarState)
Real	eps_liq_start (from BaseStructured)
Real[:]	hu_stat (from BaseStructured)
Boolean	wettedInitial (from BaseStructured)
FilmModel	filmModel

Name	Description
Geometry
FilmModel

modelTwoPhaseVarState

Parameters

Components

Contents