Fluid flow and heat transfer in capillary tubes (Stokes’ boundary-layer thickness nearly equal to the tube radius), subject to oscillatory flow from two reservoirs maintained at different temperatures, has been analyzed. Extension of existing analysis has been made by allowing for finite wall thickness and estimating the viscous dissipation. For a bundle of tubes connected to reservoirs of finite volume, analysis is also made of the oscillatory motion in the reservoirs (assuming a piston-type displacement within the reservoirs). The effects of various fluid and tube parameters on the heat transfer in a single tube are examined. The pathlines followed by fluid particles show that the extent of interaction between the fluid exiting the bundle and the fluid in the reservoirs (or the heat transfer surfaces in the reservoirs) depends strongly on the radial position of the exiting fluid particles. In a follow-up paper, these predictions are compared with some experimental results.
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Performance of a Heat Exchanger Based on Enhanced Heat Diffusion in Fluids by Oscillation: Analysis
M. Kaviany
M. Kaviany
Department of Mechanical Engineering and Applied Mechanics, The University of Michigan, Ann Arbor, MI 48109
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M. Kaviany
Department of Mechanical Engineering and Applied Mechanics, The University of Michigan, Ann Arbor, MI 48109
J. Heat Transfer. Feb 1990, 112(1): 49-55 (7 pages)
Published Online: February 1, 1990
Article history
Received:
October 18, 1988
Online:
May 23, 2008
Citation
Kaviany, M. (February 1, 1990). "Performance of a Heat Exchanger Based on Enhanced Heat Diffusion in Fluids by Oscillation: Analysis." ASME. J. Heat Transfer. February 1990; 112(1): 49–55. https://doi.org/10.1115/1.2910363
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