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TECHNICAL PAPERS: Forced Convection

Laminar Fluid Flow and Heat Transfer in a Lid-Driven Cavity Due to a Thin Fin

[+] Author and Article Information
Xundan Shi, J. M. Khodadadi

Mechanical Engineering Department, Auburn University, 201 Ross Hall, Auburn, AL 36849-5341

J. Heat Transfer 124(6), 1056-1063 (Dec 03, 2002) (8 pages) doi:10.1115/1.1517272 History: Received March 21, 2002; Revised August 12, 2002; Online December 03, 2002
Copyright © 2002 by ASME
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References

Figures

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Physical geometry and the coordinate system
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Steamlines and temperature fields for the lid-driven cavity without fins for Re=500, 1000, and 2000 (contour level increments of the primary vortex and temperature are 0.1 and 0.05, respectively)
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Flow fields for fins at different positions with Re=500: (a) l=0.05, (b) l=0.1, and (c) l=0.15
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Flow fields for fins at different positions with Re=2000: (a) l=0.05, (b) l=0.1, and (c) l=0.15
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Temperature fields for fins at different positions with Re=2000: (a) l=0.05, (b) l=0.1, and (c) l=0.15 (contour level increment of 0.05)
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Variation of the Nusselt number along four walls of the cavity with fins at different positions (Re=2000,l=0.15)
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Variation of NNR for every wall with fin’s position (Re=2000,l=0.15)
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Variation of the mean Nusselt number with positions of fins: (a) l=0.05, (b) l=0.1, and (c) l=0.15
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Curve fittings for the mean Nusselt number

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