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TECHNICAL PAPERS: Porous Media

Estimation of Average and Local Heat Transfer in Parallel Plates and Circular Ducts Filled With Porous Materials

[+] Author and Article Information
A. Haji-Sheikh

Department of Mechanical and Aerospace Engineering, The University of Texas at Arlington, Arlington, Texas 76019-0023

J. Heat Transfer 126(3), 400-409 (Jun 16, 2004) (10 pages) doi:10.1115/1.1735769 History: Received July 29, 2003; Revised February 20, 2004; Online June 16, 2004
Copyright © 2004 by ASME
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References

Nield, D. A., and Bejan, A., 1999, Convection in Porous Media, 2nd ed., Springer-Verlag, New York.
Kaviany, K., 1991, Principles of Heat Transfer in Porous Media, Springer-Verlag, New York.
Vafai, K., ed., 2000, Handbook of Porous Media, Marcel Dekker, New York.
Nield,  D. A., Kuznetsov,  A. V., and Xiong,  M., 2003, “Thermally Developing Forced Convection in a Porous Medium: Parallel Plate Channel With Walls at Uniform Temperature, With Axial Conduction and Viscous Dissipation Effects,” Int. J. Heat Mass Transfer, 46, pp. 643–651.
Beck, J. V., Cole, K., Haji-Sheikh, A., and Litkouhi, B., 1992, Heat Conduction Using Green’s Functions, Hemisphere Publ. Corp., Washington D.C.
Haji-Sheikh,  A., and Vafai,  K., 2004, “Analysis of Flow and Heat Transfer in Porous Media Imbedded Inside Various-Shaped Ducts,” Int. J. Heat Mass Transfer, 47, pp. 1889–1905.
Wolfram, S., 1999, The Mathematica Book, Fourth Edition, Cambridge University Press, Cambridge, UK.
Burmeister, L. C., 1993, Convective Heat Transfer, Second Edition, John Wiley & Sons, Inc., New York.

Figures

Grahic Jump Location
Schematic of a flow (a) parallel plate channel and (b) circular pipe
Grahic Jump Location
A comparison of data from correlation with the computed data for average heat transfer coefficient: (a) in parallel plate channels; and (b) in circular pipes.
Grahic Jump Location
Errors in the Value of N̄uD*: (a) in parallel plate channels using Eqs. (11a–b); and (b) in circular pipes using Eqs. (23,24).
Grahic Jump Location
A comparison of data from correlation with the computed data for local heat transfer coefficient: (a) in parallel plate channels; and (b) in circular pipes.
Grahic Jump Location
Errors in the Value of NuD*: (a) in parallel plate channels using Eqs. (27,28); and (b) in circular pipes using Eqs. (31,32).

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