The mechanism of the flow of gas in a fluidized bed at low pressure could be presumed from the formal analogy to the flow of gas in a capillary, but there had been no work reported on it. In order to make a contribution to the studies on the behavior of the fluidized bed at low pressure, the present work was carried out experimentally with the apparatus whose schematic diagram is shown in Fig. 1. Sifted sand, silica gel and glass beads were used as material samples and the operating conditions covered the range of pressures from 1 to 760mmHg, and that of linear velocities of gas from 10 to 250cm/secThe results obtained may be summarized as follows:(1) The behavior of the fluidized bed at low pressure has a resemblance to that at atmospheric pressure.(2) It is more difficult to have a uniform fluidized bed at low pressure than at atmospheric pressure. χ, the ratio of ΔP to the gravitational force of the bed, falls between 0.85 and 0.95 as shown in Fig. 5.(3) The relation between the pressure drop and the flow velocity through the bed at low pressure can be correlated with modified friction factor, f'' (comprizing F(e), φ and the effect of slip-flow), in the experimental region of the present work, as shown in Figs. 7 and 8.(4) The minimum flow rate for fluidization is found to decrease proportionally with the decrease in operating pressure as shown in Eq. (1); however, at a pressure lower than 100mmHg or so, no such linear relationship is found. Consequently, the corrected relation between the minimum flow rate for fluidization and pressure is proposed as given by Eq. (8), where the correction factor, J, has been obtained by correlating the conductance of capillary in the medium vacuum region. The experimental results from which Eq. (7) and J value for dpP have been obtained are shown in Figs. 9 and 10.
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