An experimental study of steam condensation on subcooled liquid films in countercurrent flow has been conducted in a small inclined test apparatus having a rectangular cross-section. Condensation heat transfer coefficients were determined and the dependence on steam and water flow rates, the degree of subcooling, and test section inclination were all studied. The results were correlated in terms of local parameters for the complete penetration and bypass regions. It was found that the local Nusselt number increases with steam and liquid Reynolds numbers and liquid Prandtl number when no bypass occurs. In the bypass region the Nusselt number drops sharply due to the strong effects of the reduced liquid film flow rate. It is shown that the local heat transfer coefficient may be related to the turbulence intensity in the liquid film which suggests that a general turbulence-centered model can be constructed.
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Experimental Study of Countercurrent Steam Condensation
A. Segev,
A. Segev
Battelle Columbus Laboratories, 505 King Avenue, Columbus, Ohio 43201
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L. J. Flanigan,
L. J. Flanigan
Battelle Columbus Laboratories, 505 King Avenue, Columbus, Ohio 43201
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R. E. Kurth,
R. E. Kurth
Battelle Columbus Laboratories, 505 King Avenue, Columbus, Ohio 43201
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R. P. Collier
R. P. Collier
Battelle Columbus Laboratories, 505 King Avenue, Columbus, Ohio 43201
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A. Segev
Battelle Columbus Laboratories, 505 King Avenue, Columbus, Ohio 43201
L. J. Flanigan
Battelle Columbus Laboratories, 505 King Avenue, Columbus, Ohio 43201
R. E. Kurth
Battelle Columbus Laboratories, 505 King Avenue, Columbus, Ohio 43201
R. P. Collier
Battelle Columbus Laboratories, 505 King Avenue, Columbus, Ohio 43201
J. Heat Transfer. May 1981, 103(2): 307-311 (5 pages)
Published Online: May 1, 1981
Article history
Received:
June 20, 1980
Online:
October 20, 2009
Citation
Segev, A., Flanigan, L. J., Kurth, R. E., and Collier, R. P. (May 1, 1981). "Experimental Study of Countercurrent Steam Condensation." ASME. J. Heat Transfer. May 1981; 103(2): 307–311. https://doi.org/10.1115/1.3244458
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