Powder Technology, Vol.277, 268-274, 2015
Effects of reducing the reactor diameter on the fluidization of a very dense powder
The impact of decreasing the column diameter from 5 to 2 cm has been studied on the fluidization of a very dense powder both at ambient and high temperature. The final objective was to coat very dense nuclear fuel particles with silicon using a Fluidized Bed Chemical Vapor Deposition (FB-CVD) process with bed weights as low as possible. A surrogate tungsten powder, 19300 kg/m(3) in density, was used. Wall effects only appeared in the column with a 2 cm diameter. This was evidenced by an increase in the hysteretic behavior of the pressure drop curves and an increase of the minimum fluidization velocity, as well as by a decrease in the bed voidage. This critical diameter is higher than those found elsewhere for Geldart's group A and B powders, which is probably due to the very high density of the tungsten powder that increases the friction forces in the bed. Satisfactory thermal conditions were reached at 650 degrees C in a reactor with a 3 cm diameter using only 740 g of powder, thereby opening the way for future silicon coating experiments. (C) 2015 Elsevier B.V. All rights reserved.
Keywords:Fluidized bed;Wall effects;Very dense particles;Minimum fluidization velocity;Pressure drop;Bed expansion