Springer Online Journal Archives 1860-2000
Chemistry and Pharmacology
Process Engineering, Biotechnology, Nutrition Technology
Conclusions 1. An experimental study has been carried out of the effects of gas flow rate, size and density of catalyst and heat-transfer-agent particles, and specific loading of the apparatus with respect to heat-transfer agent, on the concentration of settling-out particles in a fluidized bed. 2. It is shown that the experimental values of the concentration of settling heat-transfer agent particles in the fluidized bed agree well with values calculated using a modification of Stokes' equation.
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