modelGenericHumidifier_u

Steam or adiabatic humidifier with relative mass flow rate as input

Extends from AixLib.Fluid.Interfaces.TwoPortHeatMassExchanger (Partial model transporting one fluid stream with storing mass or energy).

Information

Model for an air humidifier.

This model adds moisture to the air stream. The moisture can be either liquid (adiabatic) or steam. If steam is chosen, the vaporization temperature can be fixed or calculated from the pressure.

The amount of added moisture is equal to

wat = u ṁwat,nom,

where u is the control input signal and wat,nom is equal to the parameter mWat_flow_nominal. The parameter mWat_flow_nominal must be positive.

Twater_in is used to calculate the thermal power for the vaporization (sensible and latent heat) of the steam humidifier and to calculate the enthalpy for the liquid in the adiabatic case.

Parameters

TypeNameDefaultDescription
BooleanhomotopyInitialization (from TwoPortHeatMassExchanger)true= true, use homotopy method
Modelica.Units.SI.MassFlowRatemWat_flow_nominalWater mass flow rate at u=1, positive for humidification
Modelica.Units.SI.TemperatureTLiqWat_inTemperature of liquid water that is vaporized
BooleansteamHumidifiertrueTrue: steam humidifier, false: adiabatic (water) humidifier
Assumptions
BooleanallowFlowReversal (from PartialTwoPort)true= false to simplify equations, assuming, but not enforcing, no flow reversal
Nominal condition
Modelica.Units.SI.MassFlowRatem_flow_nominal (from PartialTwoPortInterface)Nominal mass flow rate
Modelica.Units.SI.PressureDifferencedp_nominal (from TwoPortFlowResistanceParameters)Pressure difference
Advanced
Modelica.Units.SI.MassFlowRatem_flow_small (from PartialTwoPortInterface)1E-4*abs(m_flow_nominal)Small mass flow rate for regularization of zero flow
Advanced › Diagnostics
Booleanshow_T (from PartialTwoPortInterface)false= true, if actual temperature at port is computed
Flow resistance
BooleancomputeFlowResistance (from TwoPortFlowResistanceParameters)true=true, compute flow resistance. Set to false to assume no friction
Booleanfrom_dp (from TwoPortFlowResistanceParameters)false= true, use m_flow = f(dp) else dp = f(m_flow)
BooleanlinearizeFlowResistance (from TwoPortFlowResistanceParameters)false= true, use linear relation between m_flow and dp for any flow rate
RealdeltaM (from TwoPortFlowResistanceParameters)0.1Fraction of nominal flow rate where flow transitions to laminar
Dynamics › Nominal condition
Modelica.Units.SI.Timetau (from TwoPortHeatMassExchanger)30Time constant at nominal flow (if energyDynamics <> SteadyState)
Dynamics › Conservation equations
Modelica.Fluid.Types.DynamicsenergyDynamics (from TwoPortHeatMassExchanger)Modelica.Fluid.Types.Dynamics.DynamicFreeInitialType of energy balance: dynamic (3 initialization options) or steady state
Initialization
Medium.AbsolutePressurep_start (from TwoPortHeatMassExchanger)Medium.p_defaultStart value of pressure
Medium.TemperatureT_start (from TwoPortHeatMassExchanger)Medium.T_defaultStart value of temperature
Medium.MassFraction[Medium.nX]X_start (from TwoPortHeatMassExchanger)Medium.X_defaultStart value of mass fractions m_i/m
Medium.ExtraProperty[Medium.nC]C_start (from TwoPortHeatMassExchanger)fill(0, Medium.nC)Start value of trace substances
Advanced › Vaporization
BooleanTVapFixedtrueTrue: fixed vaporization temperature, false: vaporization temperature from pressure
Modelica.Units.SI.TemperatureTVap373.15Vaporization temperature of steam

Connectors

TypeNameDefaultDescription
Modelica.Fluid.Interfaces.FluidPort_aport_a (from PartialTwoPort)Fluid connector a (positive design flow direction is from port_a to port_b)
Modelica.Fluid.Interfaces.FluidPort_bport_b (from PartialTwoPort)Fluid connector b (positive design flow direction is from port_a to port_b)
Modelica.Blocks.Interfaces.RealInputuControl input
Modelica.Blocks.Interfaces.RealOutputmWat_flowWater added to the fluid
Modelica.Blocks.Interfaces.RealOutputpowerEvaConsumed power for evaporization

Components

TypeNameDefaultDescription
Modelica.Units.SI.MassFlowRatem_flow (from PartialTwoPortInterface)port_a.m_flowMass flow rate from port_a to port_b (m_flow > 0 is design flow direction)
Modelica.Units.SI.PressureDifferencedp (from PartialTwoPortInterface)port_a.p - port_b.pPressure difference between port_a and port_b
Medium.ThermodynamicStatesta_a (from PartialTwoPortInterface)if allowFlowReversal then Medium.setState_phX(port_a.p, noEvent(actualStream(port_a.h_outflow)), noEvent(actualStream(port_a.Xi_outflow))) else Medium.setState_phX(port_a.p, noEvent(inStream(port_a.h_outflow)), noEvent(inStream(port_a.Xi_outflow)))Medium properties in port_a
Medium.ThermodynamicStatesta_b (from PartialTwoPortInterface)if allowFlowReversal then Medium.setState_phX(port_b.p, noEvent(actualStream(port_b.h_outflow)), noEvent(actualStream(port_b.Xi_outflow))) else Medium.setState_phX(port_b.p, noEvent(port_b.h_outflow), noEvent(port_b.Xi_outflow))Medium properties in port_b
AixLib.Fluid.MixingVolumes.MixingVolumevol (from TwoPortHeatMassExchanger)
AixLib.Fluid.FixedResistances.PressureDroppreDro (from TwoPortHeatMassExchanger)Flow resistance
Modelica.Blocks.Sources.RealExpressionsteamEnthalpyFlow
Modelica.Blocks.Sources.RealExpressionwaterEnthalpyFlow
Modelica.Thermal.HeatTransfer.Sources.PrescribedHeatFlowprescribedHeatFlow
Modelica.Blocks.Sources.RealExpressionTVapPoint
Modelica.Blocks.Sources.RealExpressionTVapPointFix
Modelica.Blocks.Routing.RealPassThroughTsteam
Modelica.Blocks.Sources.RealExpressionrealExpression
Modelica.Blocks.Math.Productproduct

Revisions

  • December 06, 2022, by EBC-Modelica group:
    Fixes to increase compatability to OpenModelica #1378.
  • October 22, 2019, by Alexander Kümpel:
    First implementation.