4.7 Article

Comprehensive investigation of solid and porous fins influence on natural convection in an inclined rectangular enclosure

Journal

INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER
Volume 133, Issue -, Pages 729-744

Publisher

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.ijheatmasstransfer.2018.12.156

Keywords

Natural convection; Rectangular enclosure; Porous fins; Relative thermal conductivity ratio

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A numerical analysis has been performed to investigate two-dimensional natural convection inside a differentially heated inclined rectangular enclosure with several porous fins attached to the hot wall. Various parameters were studied including Rayleigh number (10(3) <= Ra <= 10(6)), Darcy number. (10(-8) <= Da <= 10(-2)), relative thermal conductivity ratio of solid phase to fluid (1 <= K-e <= 100), cavity inclination angle (0 <= phi <= pi/3), cavity aspect ratio (AR = 2:1 and 3:1), fin number (0 <= N <= 4), dimensionless fin position (0.25 <= S <= 0.75) and dimensionless fin length (0.25 <= L <= 0.75). Left vertical wall is maintained at a higher temperature T-h, while the right vertical wall is kept at lower temperature T-c and horizontal walls are insulated. Cavity is filled with an incompressible Newtonian fluid with Prandtl number of 0.71. Fins with length of l(f) are attached to the hot vertical wall. Due to a small temperature difference between the hot and cold vertical walls, all of the thermo-physical properties, except the density variation in the body force term, which is modeled using the Boussinesq approximation, are assumed constant. Governing steady state equations for mass, momentum and energy within the porous fin is based on volume-averaging method and the finite volume code based on SIMPLE method was utilized in the present investigation to solve the governing equations. The investigated results illustrated that using several conductive porous fins, increase the average Nusselt number within the cavity up to 41% compared to enclosures with solid fins and up to 20% compared to cavities without any fins. Furthermore, it was found that increasing heat transfer using more porous fins highly depends on the relative thermal conductivity ratio of solid phase to fluid and rising the thermal conductivity ratio from 10 to 100, results in 17% of heat transfer enhancement. It was found that Da = 10(-5) is a limit for positive performance of the porous fins, below which no heat transfer enhancement occurs compared to cavities with solid fins. Optimum porous fin length was found to be a decreasing function of Rayleigh number. (C) 2018 Elsevier Ltd. All rights reserved.

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