Flow in a Channel With Longitudinal Tubes

[+] Author and Article Information
C. Y. Wang

Department of Mechanical Engineering, National University of Singapore, Singapore, 119260Professor, Departments of Mathematics and Mechanical Engineering, Michigan State University, East Lansing, MI 48824

J. Fluids Eng 123(1), 157-160 (Sep 07, 2000) (4 pages) doi:10.1115/1.1335496 History: Received July 18, 2000; Revised September 07, 2000
Copyright © 2001 by ASME
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Johannsen, K., 1983, “Longitudinal flow over tube bundles,” Low Reynolds Number Flow Heat Exchangers, S. Kakac, R. K. Shah, and A. E. Bergles, eds., Hemisphere, Washington, pp. 229–273.
Shah, R. K., and London, A. L., 1978, Laminar Flow Forced Convection in Ducts, Academic, New York.
Blevins, R. D., 1984, Applied Fluid Dynamics Handbook, Van Nostrand, New York.


Grahic Jump Location
Extrapolation for small b. Circles from right: b=10−2,10−3,10−4,10−5,10−7,10−9,10−11,10−15.
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Decreased flow S due to a single cylinder. Dashed line is from Eq. (23).
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Flow per width Q versus half period λ. Dashed lines are from Eq. (24). Circles are touching cases.
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(a) Constant velocity lines λ=1.2, b=0.5, (b) λ=0.6, b=0.5, (c) λ=1, b=0.01
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(a) Cross section of the channel flow (b) domain decompositions




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