Natural Convective Heat Transfer From the Horizontal Isothermal Surface of Polygons of Octagonal and Hexagonal Shapes

Author:

Kalendar Ahmad1,Kalendar Abdulrahim2,Alhendal Yousuf2,Karar Sayed1,Alenzi Adel3,Oosthuizen Patrick4

Affiliation:

1. Department of Mechanical Power and Refrigeration Technology, College of Technological Studies-PAAET, Shuwaikh 24758, Kuwait

2. Department of Mechanical Power and Refrigeration Technology, College of Technological Studies-PAAET, Shuwaikh 24758, Kuwait e-mail:

3. Department of Chemical Engineering Technology, College of Technological Studies-PAAET, Shuwaikh 24758, Kuwait e-mail:

4. Department of Mechanical and Materials Engineering, Queen’s University, Kingston, ON, K7L 3N6, Canada e-mail:

Abstract

Heat transfer often occurs effectively from horizontal elements of relatively complex shapes in natural convective cooling of electronic and electrical devices used in industrial applications. The effect of complex surface shapes on laminar natural convective heat transfer from horizontal isothermal polygons of hexagonal and octagonal flat surfaces facing upward and downward of different aspect ratios has been numerically investigated. The polygons’ surface is embedded in a large surrounding plane adiabatic surface, where the adiabatic surface is in the same plane as the surface of the heated element. For the Boussinesq approach used in this work, the density of the fluid varies with temperature, which causes the buoyancy force, while other fluid properties are assumed constants. The numerical solution of the full three-dimensional form of governing equations is obtained by using the finite volume method-based computational fluid dynamics (CFD) code, FLUENT14.5. The solution parameters include surface shape, dimensionless surface width, different characteristic lengths, the Rayleigh number, and the Prandtl number. These parameters are considered as follows: the Prandtl number is 0.7, the Rayleigh numbers are between 103 and 108, and for various surface shapes the width-to-height ratios are between 0 and 1. The effect of different characteristic lengths has been investigated in defining the Nusselt and Rayleigh numbers for such complex shapes. The effect of these parameters on the mean Nusselt number has been studied, and correlation equations for the mean heat transfer rate have been derived.

Publisher

ASME International

Subject

Fluid Flow and Transfer Processes,General Engineering,Condensed Matter Physics,General Materials Science

Reference39 articles.

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