modelDryCooler

Cooling tower model based on epsilon-NTU relation

Extends from Buildings.Fluid.HeatExchangers.CoolingTowers.BaseClasses.CoolingTowerVariableSpeed (Base class for cooling towers with variable speed fan).

Information

Model for a steady-state or dynamic dry cooling tower with a variable speed fan using epsilon-NTU method for heat transfer.

Thermal performance

To compute the thermal performance, this model takes as parameters the nominal cooling capacity, air dry-bulb temperature, and cooling fluid (water or glycol) inlet and outlet temperatures as specified in the data record Buildings.Fluid.HeatExchangers.CoolingTowers.Data.DryCooler.Generic. The cooling tower performance is modeled using the effectiveness-NTU relationship for a crossflow configuration.

Changes in convective heat transfer coefficient on the coolant-side and the air-side due to change in flow rate and temperature are taken into account using the model Buildings.Fluid.HeatExchangers.BaseClasses.HADryCoil. This correction can be configured in the data record Buildings.Fluid.HeatExchangers.CoolingTowers.Data.DryCooler.Generic.

Parameters

TypeNameDefaultDescription
BooleanhomotopyInitialization (from TwoPortHeatMassExchanger)true= true, use homotopy method
Buildings.Fluid.HeatExchangers.CoolingTowers.Data.DryCooler.GenericdatPerformance data record
Modelica.Units.SI.ThermalConductanceUA_nominalper.UA_nominalThermal conductance at nominal flow, used to compute heat capacity
Realeps_nominalper.eps_nominalNominal heat transfer effectiveness
RealNTU_nominalper.NTU_nominalNominal number of transfer units
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)
Realn (from TwoPortFlowResistanceParameters)2Flow exponent, n=1 for laminar, n=2 for turbulent
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
Fan
Modelica.Units.SI.PowerPFan_nominal (from CoolingTowerVariableSpeed)Fan power at full speed
RealyMin (from CoolingTowerVariableSpeed)0.3Minimum control signal until fan is switched off (used for smoothing between forced and free convection regime)
cha.fanfanRelPow (from CoolingTowerVariableSpeed)Fan relative power consumption as a function of control signal, fanRelPow=P(y)/P(y=1)

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.RealOutputTLvg (from CoolingTower)Leaving water temperature
Modelica.Blocks.Interfaces.RealInputy (from CoolingTowerVariableSpeed)Fan control signal
Modelica.Blocks.Interfaces.RealOutputPFan (from CoolingTowerVariableSpeed)Electric power consumed by fan
Modelica.Blocks.Interfaces.RealInputTDryBulEntering air dry bulb temperature

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
Buildings.Fluid.MixingVolumes.MixingVolumevol (from TwoPortHeatMassExchanger)
Buildings.Fluid.FixedResistances.PressureDroppreDro (from TwoPortHeatMassExchanger)Flow resistance
Modelica.Units.SI.HeatFlowRateQ_flow (from CoolingTower)preHea.Q_flowHeat input into water circuit

Revisions

  • April 21, 2026, by Michael Wetter:
    First implementation.