Abstract
The main focus of the present paper is to apply a novel optimization algorithm called as imperialist competitive algorithm (ICA). In this algorithm the cost function being a function of input parameters has to be optimized. In the present research work, our cost function is the laminar free convection heat transfer in a horizontal cavity with adiabatic vertical and isothermally horizontal walls and adiabatic diverters. The input parameters are the diverter angle with respect to horizon varying from 0◦ to 90◦ and Rayleigh number varying from 6 × 103 to 1.2 × 104. After collecting data, the regression equation of averaged convection heat transfer is obtained as a function of the Rayleigh number and diverter angle. Subsequently, the cost function is optimized using the ICA. Results show that the proposed algorithm is powerful enough to be used for optimizing the cost function. According to the results, in order to obtain the maximum heat transfer, the diverter angle must be 27.9◦ whereas; the Rayleigh number must be 1.2 × 104.
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Abbreviations
- A :
-
Surface area of the aluminum plate (m2)
- \({A'}\) :
-
Surface area of each insulator placed right and left of the aluminum plate (m2)
- C :
-
Gladstone–Dale coefficient
- e :
-
Thickness of each diverter (mm)
- H :
-
Length of the cavity (mm)
- h y :
-
Local heat transfer coefficient (W/m2 K)
- h ave :
-
Average heat transfer coefficient (W/m2 K)
- k :
-
Thermal conductivity of air
- L :
-
Length of each diverter (mm)
- Nu y :
-
Local Nusselt number
- p :
-
Pitch of diverters (mm)
- P :
-
Pressure (Pa)
- \({q''}\) :
-
Averaged convection heat flux (W/m2)
- \({q_{{\rm cond},\, {\rm hot\,\,wall}, \,{\rm RL}}}\) :
-
Conduction heat transfer due to the contact between the hot wall and adiabatic walls (W)
- \({q_{{\rm cond}, \, {\rm hot\,\,wall},\, {\rm FB}}}\) :
-
Conduction heat transfer due to the contacts between the hot wall and insulators placed front and back of the hot wall (W)
- \({q_{{\rm conv},\, {\rm hot\,wall}}}\) :
-
Convection heat transfer obtained from the fringe patterns of the Mach–Zehnder interferometer (W)
- \({q_{{\rm cond},\,{\rm heater}}}\) :
-
Conduction heat transfer due to the contact between the heater and insulator placed below the heater (W)
- \({q_{\rm heater}}\) :
-
Power of the heater (W)
- \({q_L }\) :
-
Overall thermal dissipation (W)
- q net :
-
Absolute value of the thermal dissipation (W)
- \({q_{{\rm rad},\,{\rm hot wall}}}\) :
-
Radiation heat transfer from the hot wall (W)
- R :
-
Gas constant (J/kg K)
- Ra :
-
Rayleigh number based on the cavity side length
- T :
-
Temperature (K)
- W :
-
Cavity side length (mm)
- x :
-
Direction normal to the hot surface
- y :
-
Direction along the hot surface
- \({\varepsilon }\) :
-
Fringe shift
- \({\varepsilon '}\) :
-
Emissivity of the aluminum plate
- \({\sigma }\) :
-
Stefan–Boltzmann constant (W/(m2 K4))
- \({\alpha }\) :
-
Absorption coefficient of the aluminum plate (m2/s)
- \({\lambda}\) :
-
Laser wave length (m)
- \({\theta }\) :
-
Diverter angle (°)
- \({\Delta x}\) :
-
Thickness of each adiabatic wall (m)
- \({\Delta {x}'}\) :
-
Thickness of each insulator placed front and back of the hot wall (m)
- \({\Delta {x}''}\) :
-
Thickness of the insulator placed below the heater (m)
- col:
-
Referrers to the colony
- f:
-
Film condition
- imp:
-
Referrers to the imperialist
- pop:
-
Referrers to the population
- ref:
-
Reference condition
- Sc:
-
Cold condition
- Sh:
-
Warm condition
- \({\infty}\) :
-
Ambient condition
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Karami, A., Veysi, F., Mohebbi, S. et al. Optimization of Laminar Free Convection in a Horizontal Cavity Consisting of Flow Diverters Using ICA. Arab J Sci Eng 39, 2295–2306 (2014). https://doi.org/10.1007/s13369-013-0741-8
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DOI: https://doi.org/10.1007/s13369-013-0741-8