DIRECT CONTACT CONDENSATION OF DILUTE STEAM/AIR MIXTURES ON WAVY FALLING FILMS

Abstract Condensation from air-steam mixtures on falling water layers is investigated experimentally and theoretically. The thin film flows on the inner surface of a 5cmi.d. vertical pipe. This film is wavy turbulent while the gas phase is kept saturated with steam. Experiments are conducted with the gas mixture effectively stagnant, compared with the fast moving liquid film. Measurements are also made under a mild vacuum applied on the gas phase. Heat transfer coefficients averaged over the entire length of the condensing surface, tend to increase by decreasing the liquid flowrate, by increasing the steam fraction, and by applying a mild vacuum on the gas phase. However, for the cases examined, there is a liquid flowrate above which the heat transfer coefficient becomes almost constant. Numerical predictions are made for a fully developed turbulent film using an eddy diffusivity model. The results indicate that for a system with a large amount of noncondensable gases-as in this study-the temperature prof...

[1]  A. Karabelas,et al.  An Experimental Study of Direct-Contact Steam Condensers as Noncondensable Gas Separators , 1993 .

[2]  G. Iddan,et al.  Heat and mass transfer in condensation on the surface of a moving fluid in the presence of non-condensible gas with suction at the interface , 1971 .

[3]  A. Tamir,et al.  Interfacial heat transfer coefficients of various vapors in direct contact condensation , 1976 .

[4]  Satoru Komori,et al.  Eddy diffusivity near the free surface of open channel flow , 1977 .

[5]  A. Tamir,et al.  Direct contact condensation of an immiscible vapor on a thin film of water , 1974 .

[6]  Harold R. Jacobs Direct-Contact Condensation , 1988 .

[7]  S. G. Bankoff,et al.  Heat transfer and interfacial drag in countercurrent steam-water stratified flow , 1985 .

[8]  Ephraim M Sparrow,et al.  Condensation heat transfer in the presence of noncondensables, interfacial resistance, superheating, variable properties, and diffusion , 1966 .

[9]  Samuel Sideman,et al.  Direct Contact Condensation , 1982 .

[10]  S. Paras,et al.  Statistical characteristics of free falling films at high reynolds numbers , 1989 .

[11]  P. K. Sarma,et al.  Condensation Heat Transfer on Laminar, Falling Film , 1984 .

[12]  A. Karabelas,et al.  Surface characteristics of roll waves on free falling films , 1990 .

[13]  J. E. Crawford Condensation of a vapor in the presence of a non-condensing gas , 1959 .

[14]  G. Celata,et al.  a Theoretical and Experimental Study of Direct-Contact Condensation on Water in Turbulent Flow , 1989 .

[15]  S. Kato,et al.  Longitudinal flow characteristics of vertically falling liquid films without concurrent gas flow , 1980 .

[16]  J. L. Bravo,et al.  Distillation columns containing structured packing , 1990 .

[17]  S. G. Bankoff,et al.  Local condensation rates in nearly horizontal stratified countercurrent flow of steam and cold water , 1983 .

[18]  M. A. El-Masri,et al.  Momentum and heat transfer across freely-falling turbulent liquid films , 1986 .

[19]  R. F. Boehm,et al.  Direct-Contact Heat Transfer , 1988 .

[20]  G. Zabaras Studies of vertical annular gas-liquid flows , 1985 .