By P. Basu
This quantity specializes in the current prestige of circulating fluidized mattress expertise and offers layout details now not on hand in different places. components lined comprise combustion of fossil gasoline, hydrodynamics, combustion and environmental toxins, layout and working studies, warmth move and hydrodynamics, and strategy functions.
Read or Download Circulating Fluidized Bed Technology. Proceedings of the First International Conference on Circulating Fluidized Beds, Halifax, Nova Scotia, Canada, November 18–20, 1985 PDF
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Additional resources for Circulating Fluidized Bed Technology. Proceedings of the First International Conference on Circulating Fluidized Beds, Halifax, Nova Scotia, Canada, November 18–20, 1985
Example text
1) which had previously been discarded due to its excessively small contents of mercury. Densification of particles population by solids recycle, as noticed by early measurements (Squires, 1975) introduced a new dimension of improvement to the otherwise extremely lean constitution of dilutephase operations. Thus, fast fluidization, in addition to the dilute-phase technique mentioned above, and supplemented by shallow fluidized bed also under development in this Institute, have been 33 34 Circulating Fluidized Bed Technology grouped under the general area of "bubble-less gas/solid contacting" (Kwauk, 1983) which is a major thrust in gas fluidization studies at ICM.
1983) in Fluidization IV. ed. D. Kunii and R. Toei. Eng. Fnd. p. E. E. W. , Symp. Ser. 74, No. , and Donsi, G. (1974) Quad. Ing. Chim. Ital. 10, 185 Farrokhalaee, T. and Clift, R. (1980) in "Fluidization" ed. R. M. R. R. and Harrison, D. (1968) in "Fluidization" I. Chem. E. (London) Symposium series, No. 30. R. and Tuot, J. (1979) Trans. Inst. Chem. Engrs. J. (1961) Brit. Chem. Eng. F. W. (1961) Trans. Inst. Chem. Engrs. (London) 39, 202 Hetsroni, G, (1982) Handbook of Multiphase Systems, Hemisphere Pub.
Symp. , 73, No. , and Liss, B. E. Symp. Ser. 74, No. A. F. Y. p. 283 NOTATION D g G Bed diameter Acceleration due to gravity Solids circulation flux m m/s kg/m s H U U Bed height Superficial gas velocity Superficial gas velocity at maximum amplitude of pressure fluctuations Superficial gas velocity at onset of choking m m/s m/s Superficial gas velocity marking the point at which the amplitude of pressure fluctuations levels out at low value m/s V Slip velocity Particle terminal velocity m/s m/s ε Voidage U U U SLIP m/s ε Voidage at onset of choking p Gas density kg/m p Particle density kg/m p Mean solids hold-up kg/m P 3 ACKNOWLEDGEMENT The authors wish to thank the Science and Engineering Research Council for the financial support which has made possible the experimental work at Bradford University.