modelMS

Maxwell-Stefan mass transfer - no film reaction

Extends from SprayColumn.BaseNonEqType, ThermalSeparation.FilmModel.BaseClasses.MaxwellStefan (Maxwell-Stefan equations, no film reaction).

Parameters

TypeNameDefaultDescription
IntegernSL (from BaseFilmModel)MediumLiquid.nSubstance
IntegernSV (from BaseFilmModel)MediumVapour.nSubstance
BooleanenableDialog (from BaseFilmModel)true
BooleanStartUp_CCS (from BaseFilmModel)false
BooleanEQ (from BaseFilmModel)
BooleanMS_smooth (from MaxwellStefan)false
Integer[:]aux{1, 3, 6, 10, 15, 21, 28, 36, 45}
Propagated from Column › These variables are propagated from the column model and do not have to be set by the user!
Integernn (from BaseFilmSpray)
Boolean[nSV]inertVapour (from BaseFilmModel)fill(false, nSV)
Boolean[nSL]inertLiquid (from BaseFilmModel)fill(false, nSL)
Integern (from BaseFilmModel)
IntegernS (from BaseFilmModel)
Integer[nS,2]mapping (from BaseFilmModel){{i, i} for i in 1:nS}
SI.TemperatureT_ref (from BaseFilmModel)
BooleanconsiderStartUp (from BaseFilmModel)false
SI.Timedelay_startUp (from BaseFilmModel)200
Booleansmooth_startUp (from BaseFilmModel)false
Boolean[nSV]lowBoilingPoint (from BaseFilmModel)fill(false, nSV)

Components

TypeNameDefaultDescription
SI.Diameter[nn]d_drop (from BaseFilmSpray)
Real[nn]n_drop (from BaseFilmSpray)
Geometrygeometry (from BaseFilmSpray)
MediumVapour.ThermodynamicPropertiespropsVap (from BaseFilmModel)
SI.MoleFraction[n,nSV]x_v_star (from BaseFilmModel)
MediumVapour.ThermodynamicStatestateVap (from BaseFilmModel)
SI.MoleFraction[nSV]x_v_in (from BaseFilmModel)
SI.Concentration[n,nSV]c_v_star (from BaseFilmModel)
SI.MoleFraction[n,nSL]x_l (from BaseFilmModel)
SI.MoleFraction[n,nSV]x_v (from BaseFilmModel)
SI.Pressure[n,nSL]p_sat (from BaseFilmModel)
MediumLiquid.ThermodynamicPropertiespropsLiq (from BaseFilmModel)
MediumLiquid.ThermodynamicStatestateLiq (from BaseFilmModel)
SI.MoleFraction[n,nSL]x_l_star (from BaseFilmModel)
SI.Concentration[n,nSL]c_l (from BaseFilmModel)
SI.Concentration[n,nSL]c_l_star (from BaseFilmModel)
Real[n,nSL]eta_comp (from BaseFilmModel)
Real[n,nSL]gamma (from BaseFilmModel)
SI.MoleFraction[n,nS]x_vap_liq (from BaseFilmModel)
SI.Concentration[nSV]c_v_in (from BaseFilmModel)
SI.Concentration[n,nSV]c_v (from BaseFilmModel)
SI.VolumeFlowRateVdot_v_in (from BaseFilmModel)
SI.VolumeFlowRate[n]Vdot_v (from BaseFilmModel)
SI.VolumeFlowRate[n]Vdot_l (from BaseFilmModel)
Real[n]eps_liq (from BaseFilmModel)
SI.MolarFlowRate[n,nSL]Ndot_l_transfer (from BaseFilmModel)
SI.MolarFlowRate[n,nSV]Ndot_v_transfer (from BaseFilmModel)positive when entering the bulk phase
SI.HeatFlowRate[n]Edot_l_transfer (from BaseFilmModel)
SI.HeatFlowRate[n]Edot_v_transfer (from BaseFilmModel)
SI.Pressure[n + 1]p_hyd (from BaseFilmModel)
SI.Pressure[n + 1]p_v (from BaseFilmModel)
SI.Temperature[n]T_star (from BaseFilmModel)
Real[n]omega (from BaseFilmModel)
Boolean[n]startUp (from BaseFilmModel)
Boolean[n]before_transition (from BaseFilmModel)
Realk (from BaseFilmModel)
Real[n,nSL]rel_dev_liq (from BaseFilmModel)relative deviation from equilibrium, liquid
Real[n,nSV]rel_dev_vap (from BaseFilmModel)relative deviation from equilibrium, vapour
Realmax_rel_dev_liq (from BaseFilmModel)max(rel_dev_liq)maximum relative deviation from equilibrium, liquid
Realmax_rel_dev_vap (from BaseFilmModel)max(rel_dev_vap)maximum relative deviation from equilibrium, vapour
HomotopyMethodhomotopyMethod (from BaseFilmModel)
SI.Density[n]rho_v (from MaxwellStefan)propsVap.rho
SI.MolarMass[n]MM_v (from MaxwellStefan)propsVap.MM
ThermoEquilibrium[n]thermoEquilibrium (from MaxwellStefan)
Real[n,nS]K (from MaxwellStefan)equilibrium constant
StateSelectionstateSelection (from MaxwellStefan)
MediumLiquid.ThermodynamicFactor[n]thermoFactorL (from MaxwellStefan)
MediumVapour.ThermodynamicFactor[n]thermoFactorV (from MaxwellStefan)
MediumLiquid.CalcSpecificEnthalpy[n]liqToFilmB (from MaxwellStefan)
MediumLiquid.CalcSpecificEnthalpy[n]filmToLiqB (from MaxwellStefan)
MediumVapour.CalcSpecificEnthalpy[n]vapToFilmB (from MaxwellStefan)
MediumVapour.CalcSpecificEnthalpy[n]filmToVapB (from MaxwellStefan)
SI.CoefficientOfHeatTransfer[n]alphaLiq (from MaxwellStefan)
SI.CoefficientOfHeatTransfer[n]alphaVap (from MaxwellStefan)
Real[n,nSV,nSV]k_v (from MaxwellStefan)
Real[n,nSL,nSL]k_l (from MaxwellStefan)
SI.Area[n]A_I (from MaxwellStefan)interfacial area
MaxwellStefanMatrixmaxwellStefanMatrixVap (from MaxwellStefan)
MaxwellStefanMatrixmaxwellStefanMatrixLiq (from MaxwellStefan)
Real[n,nSL - 1,nSL - 1]R_l (from MaxwellStefan)maxwellStefanMatrixLiq.matrix
Real[n,nSV - 1,nSV - 1]R_v (from MaxwellStefan)maxwellStefanMatrixVap.matrix
InterfacialAreainterfacialArea
MassTransferCoeffVapmassTransferCoeffVap
MassTransferCoeffLiqmassTransferCoeffLiq
HeatTransferVapourheatTransferCoeffVap
HeatTransferLiquidheatTransferCoeffLiq
ThermalSeparation.Units.CoefficentOfMassTransfer[n]k_av_liq
ThermalSeparation.Units.CoefficentOfMassTransfer[n]k_av_vap
SI.DiffusionCoefficient[n]D_av_liq
SI.DiffusionCoefficient[n]D_av_vap
MediumLiquid.DiffusionCoefficientdiffCoeffLiq
SI.DiffusionCoefficient[n,aux[nSL - 1]]D_liqdiffCoeffLiq.D
MediumVapour.DiffusionCoefficientdiffCoeffVap
SI.DiffusionCoefficient[n,aux[nSV - 1]]D_vapdiffCoeffVap.D
SI.Velocity[n]w_sup_lsuperficial liquid velocity
SI.Velocity[n]w_sup_vsuperficial vapour velocity

Contents

NameDescription
InterfacialArea
MassTransferCoeffVap
MassTransferCoeffLiq
HeatTransferVapour
HeatTransferLiquid