A Study of Enhanced Heat and Mass Transfer From Variable Height Fin Array Undergoing Natural Convection

Author:

Dasgupta Debayan1,Pathak Kankan Kishore12,Giri Asis1

Affiliation:

1. Department of Mechanical Engineering, North Eastern Regional Institute of Science and Technology, Itanagar 791109, Arunachal Pradesh, India

2. Department of Mechanical Engineering, Girijananda Chowdhury Institute of Management and Technology, Guwahati 781017, Assam, India

Abstract

Abstract A numerical study is performed on simultaneous heat and mass transfer from a shrouded vertical nonisothermal variable height fin array, representing dehumidification process under natural convection. Fluid properties are treated as uniform, and the fluid is assigned to comply with Boussinesq approximation to include the effect of density variation with temperature and concentration. Semi-implicit method for the pressure linked equations revised (SIMPLER) algorithm is adopted to resolve pressure and velocity coupling. A detailed parametric investigation of fin spacing, variable fin height, and fin tip to shroud clearance for a range of thermal and mass Grashof number is undertaken. Results indicate that in case of smaller fin spacing, involving fin length of 0.3 m, coefficients of sensible and latent heat transfer increase with the decreasing variable height (H1*) of fin and become maximum at H1*=0.5, for all thermal and mass Grashof numbers considered presently. Further, total heat transfer analysis on a particular base length due to sensible heat shows a maximum of 24.4% enhancement, whereas same due to the latent heat shows a maximum of 25.8% enhancement, depending on the values of clearance. Induced velocities also increase with the decreasing variable height of fin (H1*), which influences the heat and mass transport. The output parameters of this analysis, like induced velocities and overall Nusselt numbers due to the sensible and latent heat, are correlated with the governing parameters. The correlation coefficients are found to be in a range from 0.97 to 0.99.

Publisher

ASME International

Subject

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

Reference42 articles.

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4. Comparison of One Dimensional and Two Dimensional Models for Wet Surface Fin Efficiency of a Plate-Fin-Tube Heat Exchanger;Liang;Appl. Therm. Eng.,2000

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