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TECHNICAL NOTES

Effect of Tube Inclination on Pool Boiling Heat Transfer

[+] Author and Article Information
M.-G. Kang

Department of Mechanical Engineering Education, Andong National University, 388 Songchun-dong, Andong-city, Kyungbuk 760-749, Korea

J. Heat Transfer 122(1), 188-192 (Oct 01, 1999) (5 pages) doi:10.1115/1.521456 History: Received January 01, 1999; Revised October 01, 1999
Copyright © 2000 by ASME
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References

Corletti, M. M., and Hochreiter, L. E., 1991, “Advanced Light Water Reactor Passive Residual Heat Removal Heat Exchanger Test,” Proceedings of the 1st JSME/ASME Joint International Conference on Nuclear Engineering, Tokyo, Japan, pp. 381–387.
Kang,  M. G., 1998, “Experimental Investigation of Tube Length Effect on Nucleate Pool Boiling Heat Transfer,” Ann. Nucl. Energy, 25, No. 4-5, pp. 295–304.
Jakob, M., and Hawkins, G. A., 1957, Elements of Heat Transfer, 3rd. ed., John Wiley and Sons, New York, pp. 206–210.
van Stralen,  S. J. D., and Sluyter,  W. M., 1969, “Investigations on the Critical Heat Flux of Pure Liquids and Mixtures Under Various Conditions,” Int. J. Heat Mass Transf., 12, pp. 1353–1384.
Nishikawa,  K., , 1984, “Effect of Surface Configuration on Nucleate Boiling Heat Transfer,” Int. J. Heat Mass Transf., 27, No. 9, pp. 1559–1571.
Chyu,  M. C., and Mghamiz,  A. M., 1991, “Nucleate Boiling on Two Cylinders in Line Contact,” Int. J. Heat Mass Transf., 34, No. 7, pp. 1783–1790.
Chun,  M. H., and Kang,  M. G., 1998, “Effects of Heat Exchanger Tube Parameters on Nucleate Pool Boiling Heat Transfer,” ASME J. Heat Transfer, 120, pp. 468–476.

Figures

Grahic Jump Location
Schematic diagram of the experimental appratus: (a) overall arrangement, (b) water storage tank and heated tube
Grahic Jump Location
Changes in heat flux and tube wall superheat due to thermocouple location: (a) horizontal tube (θ=0 deg); (b) vertical tube (θ=90 deg)
Grahic Jump Location
Bubble generation and coalescence on the heated tube surface (D=19.05 mm,ε=60.9 nm) for various heat fluxes: (a) θ=0 deg, (b) θ=45 deg, and (c) θ=90 deg
Grahic Jump Location
Effects of tube (D=19.05 mm) inclination on pool boiling heat transfer: (a) rough surface (ε=60.9 nm) and (b) smooth surface (ε=15.1 nm)

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