Fluidized beds powders

Fluidized-bed powdered activated carbon systems represent another important process. The use of activated carbon for the tertiary treatment of secondary sewage effluents has been used extensively. Powdered carbon is as effective as granular activated carbon for removing the organic impurities from the wastewater. [Pg.318]

Chang, H., and Louge, M., Fluid Dynamic Similarity of Circulating Fluidized Beds, Powder Tech., 70 259 (1992)... [Pg.105]

DiFelice, R., Rapagna, S., and Foscolo, P. U., Dynamic Similarity Rules Validity Check for Bubbling and Slugging Fluidized Beds, Powder Technol., 71 281 (1992a)... [Pg.105]

Glicksman, L. R., and McAndrews, G., The Effect of Bed Width on the Hydrodynamics of Large Particle Fluidized Beds, Powder Technol., 42 159... [Pg.106]

Herb, B. E., Dou, S., Tuzla, K., and Chen, J. C., Solid Mass Fluxes in Circulating Fluidized Beds, Powder Technol., 197-205 (1992)... [Pg.205]

Colakyan, M., and Levenspiel, O., Elutriation from Fluidized Beds, Powder Technol., 38 223 (1984)... [Pg.324]

Ettehadieh, B., Yang, W. C., and Haldipur, G. B., Motion of Solids, Jetting and Bubbling Dynamics in a Large Jetting Fluidized Bed, Powder Tech., 54 243 (1988)... [Pg.324]

Yang, W. C., and Keaims, D. L., Solid Entrainment Rate into Gas and Gas-Solid, Two-Phase Jets in a Fluidized Bed, Powder Technol., 33 89 (1982)... [Pg.329]

Levenspiel, O., Kunii, D., and Fitzgerald, T., The Processing of Solids of Changing Size in Bubbling Fluidized Beds, Powder Tech., 2 87 (1968)... [Pg.488]

Geldart, D., The Effect of Particle Size and Size Distribution on the Behavior of Gas-Fluidized Beds, Powder Technol., 6 201-205 (1972)... [Pg.578]

Boland, D., and Geldart, D., Electrostatic charging in gas fluidized beds, Powder Technol., 5 289-297 (1971/72)... [Pg.867]

Guardiola, J., Ramos, G., and Romero, A., Electrostatic behaviour in binary dielectric/conductor fluidized beds, Powder Technol., 73 11-19 (1992)... [Pg.868]

Y. Tsuji, T. Kawaguchi, T. Tanaka, Discrete particle simulation of two-dimensional fluidized bed, Powder Technol. 77 (1993) 79-87. [Pg.174]

J. Aguillon, K. Shakourzadeh, P. Guigon, A new method for local solid concentration measurements in circulating fluidized bed, Powder Technol. 86 (1996) 251-255. [Pg.312]

Stewart, P. S. B. and Davidson, J. F. (1967). Slug Flow in Fluidized Beds. Powder Tech., 1,61. Thonglimp, V. (1981). Contribution a L itude Hydrodynamique des Couches Fluidiseis pour un Gaz Vitesse Minimale de Fluidisation et Expansion. Docteur-Ingenieur thesis. Institut National Polytechnique, Toulouse. [Pg.415]

Kunii, D. and Levenspiel, 0. (1990). Entrainment of Solids from Fluidized Beds. I. Holdup of Solids in the Freeboard, n. Operation of Fast Fluidized Beds. Powder Tech., 61,... [Pg.457]

Baeyens, J. and Goossens, W. R. A. (1973). Some Aspects of Heat Transfer Between a Vertical Wall and a Gas Fluidized Bed. Powder Tech., 8, 91. [Pg.535]

Geldart D. 1972. The effect of particle size and size distribution on the behaviour of gas-fluidized beds. Powder Technol. 6(4) 201-215. [Pg.86]

Trivedi U, Bassi A, Zhu J-X (2006) Continuous enzymatic polymerization of phenol in a liquid-solid circulating fluidized bed. Powder Technol 169 61-70... [Pg.288]

Asif, M. and Ibrahim, A. A, Minimum fluidization velocity and defluidization behavior of binary-solid liquid-fluidized beds. Powder Techno 2002, 126 (3), 241-254. [Pg.1545]

Xu, M., and Turton, R. (1997), A new data processing technique for noisy signals Application to measuring particle circulation times in a draft tube equipped fluidized bed. Powder Technol., 92,111-117. [Pg.1124]

Dry, R. J. Radial concentration profiles in a fast fluidized bed, Powder Technol. 49,37-44(1987). Dry. R. J., and White, C. C. Gas residence time characteristics in a high-velocity circulating fluidized bed of FCC catalyst, Powder Techn. 58, 17 (1989). [Pg.142]

Martin, M. P, Thrlier, P, and Bertrand, J. R., Gas and solid behavior in cracking circulating fluidized beds. Powder Technol. 70,249 (1992). [Pg.324]

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