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B. Shi, R.K. AL-Dadah, S. Mahmoud, A. Elsayed and A. Rezk
Mathematical and CFD modeling for a
rectangular finned tube adsorption bed for
automotive cooling system
SusTEM Special Sessions on
Thermal Energy Management
Presentation outline
• Background
• Investigation aim
• Bed design
• Mathematical model
• CFD model
• CFD simulation results
• Result comparison
• Simulation results for desorption
• Effect of fin height and fin pitch
• Conclusions
Background
• Adsorption cooling systems in automotive applications
– Driven by engine coolant water or engine exhaust gas
• Decreasing fuel consumption
• Decreasing exhaust gas emissions
– Limited application because of large volume, high weight and low efficiency
• Advantages of water refrigerant
– High latent heat of evaporation
– Thermal stability at high temperature
– Good compatibility with wide range of materials
• Advantages of silica gel adsorbent
– Excellent thermal properties
– Low generation temperature
– High adsorption kinetics
Background
Operation concept of adsorption Chiller
Investigation aim
• This paper developed two simulation methods to investigate the
adsorption and desorption processes of a silica gel-water pair in
rectangular finned tube bed structure that can be used for automotive
application
– The lumped parameter approach to model the heat and mass transfer in the adsorptionand desorption processes
– Computational fluid technique to simulate the adsorption and desorption processes inthe bed
Symbol Value Description
Lf 275mm Bed Length
Wf 115mm Fin Width
Hf 30mm Fin Height
pf 1.5mm Fin Pitch
tf 0.105mm Fin Thickness
Do 15.875mm Tube Outer Diameter
tt 0.8mm Tube Thickness
Bed design parametersCondition Value
Initial Bed Temperature 60ºC
Evaporator Temperature 15ºC
Cooling Water Inlet Temperature 30 ºC
Cooling Water Flow Rate 30L/min
Initial Bed Pressure 1.01325kPa
Initial Uptake Rate 0.02kgwater/kgsilicagel
Adsorption Conditions
• CFD model
MATLAB with REFPROP
COMSOL Multiphysics
Bed Configuration
• Mathematical model
Mathematical model
where and
• Energy equation
• Adsorption kinetics :
dtdwTPhTehMTTCpmdtdwHM bedewwsoutincss /)],()([)(/ −+−+∆•
Mathematical model
• Calculation for thermal resistance
CFD model
CFD model
where and
• Adsorption kinetics :
• Energy equation
• Darcy equation
CFD simulation results
Temperature distributions at 600s
Temperature distribution of the last fin at 100s, 300s and 600s
Results comparison
Maximum deviation
Water uptake rate 8.2%
Average bed temperature 0.9%
Water outlet temperature 0.2%
Deviation between two models
• Both techniques can predict the dynamics of the adsorption process with reasonable deviation
Simulation results for desorption
• Results from both methods indicate good agreement
Condition Value
Initial Bed Temperature 30ºC
Heating Water Inlet Temperature 60 ºC
Heating Water Flow Rate 30L/min
Initial Bed Pressure 1.01325kPa
Initial Uptake Rate 0.02kgwater/kgsilicagel
Desorption Conditions
Effect of fin height and fin pitch-CFD Investigation
Different fin height Different fin pitch
• Decreasing the fin height results in increasing the water uptake rate by 19% from 35mm to 20mm.
• Decreasing the fin pitch results in increasing the water uptake rate by up to 8% from 3mm to 1.5mm.
Conclusions
• A mathematical model and a CFD model were developed to investigate the performance of a silica gel-water pair in rectangular finned tube bed structure that can be used for automotive application
• Simulations were used to investigate the bed performance of adsorption and desorption performance with results form both methods were very close.
• The CFD technique was used to investigate the effect of fin pitch and fin height on the performance of adsorption bed
– Decreasing the fin height results in increasing the water uptake rate
– Decreasing the fin pitch results in increasing the water uptake rate
• 12 beds (distributed between two adsorbers) will be required to provide an average of 2kW for an automotive air conditioning system
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