Abstract
A mathematical model is presented for solution granulation; the model has been tested by experiment. The model indicates that sectionalized equipment is suitable.
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G. I. Shishkin, V. F. Volkov, V. F. Egolaeva, and V. V. Ukhlov, “Sectionalization of fluidized beds,” Inzh.-Fiz. Zh.,29, No. 3 (1975).
V. F. Volkov, V. M. Pavlov, et al., Khim. Prom-st, No. 6 (1966).
V. F. Volkov, I. I. Shishko, and L. V. Khokhlova, in: Heat and Mass Transfer [in Russian], Vol. 5, Minsk (1968).
O. M. Todes, Yu. Ya. Kaganovich, et al., Fluidized-Bed Solution Evaporation [in Russian], Metallurgiya, Moscow (1973).
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Translated from Inzhenerno-Fizicheskii Zhurnal, Vol. 33, No. 4, pp. 596–602, October, 1977.
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Volkov, V.F., Shishkin, G.I., Ukhlov, V.V. et al. Sectionalized fluidized-bed equipment for solution granulation. Journal of Engineering Physics 33, 1143–1148 (1977). https://doi.org/10.1007/BF00858999
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DOI: https://doi.org/10.1007/BF00858999