modelDryCoilEffectivenessNTU

Heat exchanger with effectiveness - NTU relation and no moisture condensation

Extends from Buildings.Fluid.HeatExchangers.BaseClasses.PartialEffectivenessNTU (Partial model for heat exchanger with effectiveness - NTU relation and no moisture condensation).

Information

Model of a coil without humidity condensation. This model transfers heat in the amount of

Q̇ = Q̇max ε
ε = f(NTU, Z, flowRegime),

where max is the maximum heat that can be transferred, ε is the heat transfer effectiveness, NTU is the Number of Transfer Units, Z is the ratio of minimum to maximum capacity flow rate and flowRegime is the heat exchanger flow regime. such as parallel flow, cross flow or counter flow.

The flow regimes depend on the heat exchanger configuration. All configurations defined in Buildings.Fluid.Types.HeatExchangerConfiguration are supported.

The convective heat transfer coefficients scale proportional to (ṁ/ṁ0)n, where is the mass flow rate, 0 is the nominal mass flow rate, and n=0.8 on the air-side and n=0.85 on the water side.

For a heat and moisture exchanger, use Buildings.Fluid.MassExchangers.ConstantEffectiveness.

Parameters

TypeNameDefaultDescription
BooleanprescribedHeatFlowRate1 (from StaticFourPortHeatMassExchanger)falseSet to true if the heat flow rate into fluid 1 is not a function of the component temperature
BooleanprescribedHeatFlowRate2 (from StaticFourPortHeatMassExchanger)falseSet to true if the heat flow rate into fluid 2 is not a function of the component temperature
BooleanhomotopyInitialization (from StaticFourPortHeatMassExchanger)true= true, use homotopy method
BooleansensibleOnly1 (from StaticFourPortHeatMassExchanger)Set to true if sensible exchange only for medium 1
BooleansensibleOnly2 (from StaticFourPortHeatMassExchanger)Set to true if sensible exchange only for medium 2
Buildings.Fluid.Types.HeatExchangerConfigurationconfiguration (from PartialEffectivenessNTU)Heat exchanger configuration
Booleanuse_dynamicFlowRegime (from PartialEffectivenessNTU)falseIf true, flow regime is determined using actual flow rates
Modelica.Units.SI.ThermalConductanceUA_nominal (from PartialEffectivenessNTU)Nominal UA value
RealNTU_nominal (from PartialEffectivenessNTU)Nominal number of transfer units
Assumptions
BooleanallowFlowReversal1 (from PartialFourPort)true= false to simplify equations, assuming, but not enforcing, no flow reversal for medium 1
BooleanallowFlowReversal2 (from PartialFourPort)true= false to simplify equations, assuming, but not enforcing, no flow reversal for medium 2
Nominal condition
Modelica.Units.SI.MassFlowRatem1_flow_nominal (from PartialFourPortInterface)Nominal mass flow rate
Modelica.Units.SI.MassFlowRatem2_flow_nominal (from PartialFourPortInterface)Nominal mass flow rate
Modelica.Units.SI.PressureDifferencedp1_nominal (from FourPortFlowResistanceParameters)Pressure difference
Modelica.Units.SI.PressureDifferencedp2_nominal (from FourPortFlowResistanceParameters)Pressure difference
Advanced
Medium1.MassFlowRatem1_flow_small (from PartialFourPortInterface)1E-4*abs(m1_flow_nominal)Small mass flow rate for regularization of zero flow
Medium2.MassFlowRatem2_flow_small (from PartialFourPortInterface)1E-4*abs(m2_flow_nominal)Small mass flow rate for regularization of zero flow
Advanced › Diagnostics
Booleanshow_T (from PartialFourPortInterface)false= true, if actual temperature at port is computed
Flow resistance › Medium 1
BooleancomputeFlowResistance1 (from FourPortFlowResistanceParameters)true=true, compute flow resistance. Set to false to assume no friction
Booleanfrom_dp1 (from FourPortFlowResistanceParameters)false= true, use m_flow = f(dp) else dp = f(m_flow)
Realn1 (from FourPortFlowResistanceParameters)2Flow exponent for side 1, n=1 for laminar, n=2 for turbulent
BooleanlinearizeFlowResistance1 (from FourPortFlowResistanceParameters)false= true, use linear relation between m_flow and dp for any flow rate
RealdeltaM1 (from FourPortFlowResistanceParameters)0.1Fraction of nominal flow rate where flow transitions to laminar
Flow resistance › Medium 2
BooleancomputeFlowResistance2 (from FourPortFlowResistanceParameters)true=true, compute flow resistance. Set to false to assume no friction
Booleanfrom_dp2 (from FourPortFlowResistanceParameters)false= true, use m_flow = f(dp) else dp = f(m_flow)
Realn2 (from FourPortFlowResistanceParameters)2Flow exponent for side 2, n=1 for laminar, n=2 for turbulent
BooleanlinearizeFlowResistance2 (from FourPortFlowResistanceParameters)false= true, use linear relation between m_flow and dp for any flow rate
RealdeltaM2 (from FourPortFlowResistanceParameters)0.1Fraction of nominal flow rate where flow transitions to laminar
Nominal thermal performance
Booleanuse_Q_flow_nominal (from PartialEffectivenessNTU)trueSet to true to specify Q_flow_nominal and temperatures, or to false to specify effectiveness
Modelica.Units.SI.HeatFlowRateQ_flow_nominal (from PartialEffectivenessNTU)Nominal heat flow rate (positive for heat transfer from 1 to 2)
Modelica.Units.SI.TemperatureT_a1_nominal (from PartialEffectivenessNTU)Nominal temperature at port a1
Modelica.Units.SI.TemperatureT_a2_nominal (from PartialEffectivenessNTU)Nominal temperature at port a2
Realeps_nominal (from PartialEffectivenessNTU)Nominal heat transfer effectiveness
Heat transfer › Nominal condition
Realr_nominal2/3Ratio between air-side and water-side convective heat transfer coefficient
Heat transfer
Realn_w0.85Water-side exponent for convective heat transfer coefficient, h~m_flow^n_w
Realn_a0.8Air-side exponent for convective heat transfer coefficient, h~m_flow^n_a

Connectors

TypeNameDefaultDescription
Modelica.Fluid.Interfaces.FluidPort_aport_a1 (from PartialFourPort)Fluid connector a1 (positive design flow direction is from port_a1 to port_b1)
Modelica.Fluid.Interfaces.FluidPort_bport_b1 (from PartialFourPort)Fluid connector b1 (positive design flow direction is from port_a1 to port_b1)
Modelica.Fluid.Interfaces.FluidPort_aport_a2 (from PartialFourPort)Fluid connector a2 (positive design flow direction is from port_a2 to port_b2)
Modelica.Fluid.Interfaces.FluidPort_bport_b2 (from PartialFourPort)Fluid connector b2 (positive design flow direction is from port_a2 to port_b2)

Components

TypeNameDefaultDescription
Medium1.MassFlowRatem1_flow (from PartialFourPortInterface)port_a1.m_flowMass flow rate from port_a1 to port_b1 (m1_flow > 0 is design flow direction)
Modelica.Units.SI.PressureDifferencedp1 (from PartialFourPortInterface)port_a1.p - port_b1.pPressure difference between port_a1 and port_b1
Medium2.MassFlowRatem2_flow (from PartialFourPortInterface)port_a2.m_flowMass flow rate from port_a2 to port_b2 (m2_flow > 0 is design flow direction)
Modelica.Units.SI.PressureDifferencedp2 (from PartialFourPortInterface)port_a2.p - port_b2.pPressure difference between port_a2 and port_b2
Medium1.ThermodynamicStatesta_a1 (from PartialFourPortInterface)if allowFlowReversal1 then Medium1.setState_phX(port_a1.p, noEvent(actualStream(port_a1.h_outflow)), noEvent(actualStream(port_a1.Xi_outflow))) else Medium1.setState_phX(port_a1.p, inStream(port_a1.h_outflow), inStream(port_a1.Xi_outflow))Medium properties in port_a1
Medium1.ThermodynamicStatesta_b1 (from PartialFourPortInterface)if allowFlowReversal1 then Medium1.setState_phX(port_b1.p, noEvent(actualStream(port_b1.h_outflow)), noEvent(actualStream(port_b1.Xi_outflow))) else Medium1.setState_phX(port_b1.p, port_b1.h_outflow, port_b1.Xi_outflow)Medium properties in port_b1
Medium2.ThermodynamicStatesta_a2 (from PartialFourPortInterface)if allowFlowReversal2 then Medium2.setState_phX(port_a2.p, noEvent(actualStream(port_a2.h_outflow)), noEvent(actualStream(port_a2.Xi_outflow))) else Medium2.setState_phX(port_a2.p, inStream(port_a2.h_outflow), inStream(port_a2.Xi_outflow))Medium properties in port_a2
Medium2.ThermodynamicStatesta_b2 (from PartialFourPortInterface)if allowFlowReversal2 then Medium2.setState_phX(port_b2.p, noEvent(actualStream(port_b2.h_outflow)), noEvent(actualStream(port_b2.Xi_outflow))) else Medium2.setState_phX(port_b2.p, port_b2.h_outflow, port_b2.Xi_outflow)Medium properties in port_b2
Modelica.Units.SI.HeatFlowRateQ1_flow (from StaticFourPortHeatMassExchanger)Heat transferred into the medium 1
Medium1.MassFlowRatemWat1_flow (from StaticFourPortHeatMassExchanger)Moisture mass flow rate added to the medium 1
Modelica.Units.SI.HeatFlowRateQ2_flow (from StaticFourPortHeatMassExchanger)Heat transferred into the medium 2
Medium2.MassFlowRatemWat2_flow (from StaticFourPortHeatMassExchanger)Moisture mass flow rate added to the medium 2
Medium1.TemperatureT_in1 (from PartialEffectiveness)if allowFlowReversal1 then fra_a1*Medium1.temperature(state_a1_inflow) + fra_b1*Medium1.temperature(state_b1_inflow) else Medium1.temperature(state_a1_inflow)Inlet temperature medium 1
Medium2.TemperatureT_in2 (from PartialEffectiveness)if allowFlowReversal2 then fra_a2*Medium2.temperature(state_a2_inflow) + fra_b2*Medium2.temperature(state_b2_inflow) else Medium2.temperature(state_a2_inflow)Inlet temperature medium 2
Modelica.Units.SI.ThermalConductanceC1_flow (from PartialEffectiveness)abs(m1_flow)*(if allowFlowReversal1 then fra_a1*Medium1.specificHeatCapacityCp(state_a1_inflow) + fra_b1*Medium1.specificHeatCapacityCp(state_b1_inflow) else Medium1.specificHeatCapacityCp(state_a1_inflow))Heat capacity flow rate medium 1
Modelica.Units.SI.ThermalConductanceC2_flow (from PartialEffectiveness)abs(m2_flow)*(if allowFlowReversal2 then fra_a2*Medium2.specificHeatCapacityCp(state_a2_inflow) + fra_b2*Medium2.specificHeatCapacityCp(state_b2_inflow) else Medium2.specificHeatCapacityCp(state_a2_inflow))Heat capacity flow rate medium 2
Modelica.Units.SI.ThermalConductanceCMin_flow (from PartialEffectiveness)min(C1_flow, C2_flow)Minimum heat capacity flow rate
Modelica.Units.SI.HeatFlowRateQMax_flow (from PartialEffectiveness)CMin_flow*(T_in2 - T_in1)Maximum heat flow rate into medium 1
Modelica.Units.SI.ThermalConductanceUA (from PartialEffectivenessNTU)UA value
Realeps (from PartialEffectivenessNTU)Heat exchanger effectiveness
Buildings.Fluid.HeatExchangers.BaseClasses.HADryCoilhAModel for convective heat transfer coefficient

Revisions

  • June 22, 2026, by Michael Wetter:
    Updated Dialog annotations, and revised heat exchanger models to consistently expose parameters r_nominal, n_w and n_a.
    This is for #4620.
  • September 25, 2018, by Michael Wetter:
    Refactored model to use a common base class.