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Fluidization fluidized beds

Hartge, E.-U., Li, Y., and Werther, J., Flow Structures in Fast Fluidized Beds, Fluidization V, Proc. 5th Eng. Foundation Conf. on Fluidization, Elsinore Denmark, p. 345 (1985)... [Pg.107]

Noymer, P. D., Hyre, M. R., and Glicksman, L. R., The Influence of Bed Diameter on Hydrodynamics and Heat Transfer in Circulating Fluidized Beds, Fluidization and Fluid-Particle Systems, AIChE, pp. 86-90 (1995)... [Pg.108]

Beaude, F., and Louge, M., Similarity of Radial Profiles of Solid Volume Fraction in a Circulating Fluidized Bed, Fluidization VIII, pp. 245-253 (1995)... [Pg.203]

Dou, S., Herb, B., Tuzla, K., and Chen, J. C., Dynamic Variation of Solid Concentration and Heat Transfer Coefficient at Wall of Circulating Fluidized Bed, Fluidization VII, 793-801 (1993)... [Pg.204]

Ozkaynak, T. F., Chen, J. C., and Frankenfield, T. R., An Experimental Investigation of Radiant Heat Transfer in High Temperature Fluidized Bed, Fluidization, Fourth International Conf. on Fluidization, pp. 371— 378, Engineering Foundation (1983)... [Pg.207]

Gilbertson, M. A., Cheesman, D. J., and Yates, J. G., Observations and measurements of isolated bubbles in a pressurized gas-fluidized bed. Fluidization IX, Proceedings of the Engineering Foundation Conference on Fluidization 9 th, Durango, CO, United States, May 17-22, 61-68 (1998). [Pg.219]

Fluidized Beds Fluidized beds are reactors in which small particles (with average size below 0.1 mm) are fluidized by the reactant gases or liquids. When the linear velocity is above the minimum required for fluidization, a dense fluidized bed is obtained. As the superficial velocity increases, the bed expands and becomes increasingly dilute. At a high enough linear velocity, the smallest particles entrain from the bed and have to be separated from the exhaust gases and recycled. [Pg.33]

Balzer, G., Boelle, A. and Simonin, O. (1995), Eulerian gas-solid flow modeling of dense fluidized bed. Fluidization VIII, Int. Symp. Of the Engineering Foundation, Tours, p. 1125. [Pg.115]

Fluidized beds Fluidization of the bed can result in enhanced heat and mass transfer performance. Unfortunately, many fluidized bed designs tend to be voluminous, which reduces overall storage efficiency. [Pg.95]

Hemati, M., M. Mourad, D. Steinmetz, and C. Lagurie (1992). Continuous and intermittent drying of maize in a flotation fluidized bed. Fluidization VII. Proceedings of the Seventh Engineering Foundation Conference on Fluidization, May 3-8, 1992, Brisbane, Queensland, Australia. [Pg.501]

Noymer PD, Hyre MR, Glicksman LR. The influence of bed diameter on hydrodynamics and heat transfer in circulating fluidized beds. Fluidization and Fluid-Particle Systems, AIChE, 1995, pp 86-90. [Pg.382]

Epstein, N. and D. Nicks, "Contraction or Expansion of Three-Phase Fluidized Beds". Fluidization Technology, ed. D. Keairns 389-397 (Washington, Hemisphere Publishing Corporation 1976). [Pg.386]

Dakshinamurty, P., C. Chiranjevi, V. Subrahmanyam and P.K. Rao, "Studies of Gas-Liquid Mass Transfer in a Gas-Liquid Fluidized Bed". Fluidization and its applications 429-439 (Toulouse, Cepadues-Editions, 1973). [Pg.390]

Begovich, J.M., and Watson, J.S., "Hydrodynamic Characteristics of Three Phase Fluidized Beds", Fluidization, Eds. Davidson and Keaims, 190-195 (Cambridge, Cambridge University Press, 1978). [Pg.409]

Water often is treated in simple vessels known as batch reactors, which hold from a few hundred to many thousands of liters. Nutrients, microorganism, or both may be added to promote degradation of particular contaminants. Another variation on reactors designed for treatment of water is the fluidized bed. Fluidized beds usually contain biomass immobilized on or within carriers (e.g., polysaccharide-based beads, plastic saddles, sand particles, etc.). These carrier matrixes are circulated... [Pg.296]

Balzer G, BoeUe A, Simonin O (1995) Eulerian gas-sohd flow modelling of dense fluidized bed. Fluidization VIII, international symposium of the engineering foundation. Tours, 14-19... [Pg.679]


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