modelSteadyStateAnalysis

steady state analysis for heat exchangers

Information

Temperature distributions of the heat exchangers in cocurrent and countercurrent mode are given. T_H and T_c represent the temperature of the hot fluid and the cold fluid, respectively.

∆T represents the temperature difference between hot and cold fluids along the heat exchangers. And, x is a point along the channels of the heat exchanger. In the countercurrent mode, ∆T does not vary along the channels as much as the ∆T in the cocurrent mode. Moreover, in cocurrent mode, ∆T is very large at the inlet of the channels and getting smaller progressively. Countercurrent heat exchanger can be evaluated as more efficient with respect to cocurrent heat exchanger since countercurrent mode requires smaller heat transfer area to provide the same heat transfer rate.

At the steady state, the total flow rates of Q_A and Q_B is equal to a steady state rate equation and it is used for the verification of the models. Steady state heat rate equation for a heat exchanger is written as follows:

Q=UA∆Teog

where U is the average overall heat transfer coefficient, A is the area of the heat transfer surface and ∆Teog is the average temperature driving force. UA is described as:

UA=Lω(γ_A γ_B)/(γ_A+γ_B )

where L is the length, ω is the perimeter of the channels, γ_A and γ_B are the heat transfer coefficients of fluid A and B respectively.

∆Teog is written as:

where ∆T_L is the temperature difference of the fluids A and B at the outlet of the channels and ∆T_o is the temperature difference of the fluids A and B at the inlet of the channels.

Parameters Comment
L length of the channels
N number of nodes
wB mass flow rate of fluid B
areaA cross sectional area of channel A
areaB cross sectional area of channel B
rhoA density of fluid A
rhoB density of fluid B
cpA specific heat capacity of fluid A
cpB specific heat capacity of fluid B
cpW specific heat capacity of the wall
gammaA heat transfer coefficient of fluid A
gammaB heat transfer coefficient of fluid B
omega perimeter
UA average overall heat transfer coefficient * area of the heat transfer surface

Parameters

TypeNameDefaultDescription
SIunits.LengthL10length of the channels
IntegerN20number of nodes
SIunits.MassFlowRatewB1mass flow rate of fluid B
SIunits.AreaareaA5e-5cross sectional area of channel A
SIunits.AreaareaB5e-5cross sectional area of channel B
SIunits.DensityrhoA1000density of fluid A
SIunits.DensityrhoB1000density of fluid B
SIunits.SpecificHeatCapacitycpA4200specific heat capacity of fluid A
SIunits.SpecificHeatCapacitycpB4200specific heat capacity of fluid B
SIunits.SpecificHeatCapacitycpW2000specific heat capacity of wall
SIunits.CoefficientOfHeatTransfergammaA4000heat transfer coefficient of fluid A
SIunits.CoefficientOfHeatTransfergammaB10000heat transfer coefficient of fluid B
SIunits.Lengthomega0.1perimeter
SIunits.PerUnitUAL*omega*gammaA*gammaB/(gammaA + gammaB)

Components

TypeNameDefaultDescription
Models.CounterCurrentHeatExchangerEquationscountercur
Models.CocurrentHeatExchangerEquationscocur
SIunits.TemperaturedTeogCocuraverage temperature driving force at cocurrent mode
SIunits.TemperaturedTeogCountercuraverage temperature driving force at countercurrent mode
SIunits.HeatFlowRateQcocur_sssteady state rate equation at cocurrent mode
SIunits.HeatFlowRateQcocur_fluidAtotal heat flow rate of fluid A at cocurrent mode
SIunits.HeatFlowRateQcocur_fluidBtotal heat flow rate of fluid B at cocurrent mode
SIunits.HeatFlowRateQcountercur_sssteady state rate equation at countercurrent mode
SIunits.HeatFlowRateQcountercur_fluidAtotal heat flow rate of fluid A at countercurrent mode
SIunits.HeatFlowRateQcountercur_fluidBtotal heat flow rate of fluid B at countercurrent mode
SIunits.TemperatureP1temperature difference between fluid A and B at node N at cocurrent mode
SIunits.TemperatureP2temperature difference between fluid A and B at node 1 at cocurrent mode
SIunits.TemperatureP3temperature difference between fluid A and B at node N at countercurrent mode
SIunits.TemperatureP4temperature difference between fluid A and B at node 1 at countercurrent mode