aDepartment of Chemical Engineering Chemistry and Environmental Science, New Jersey Institute of Technology, Newark, NJ 07102, USA
bDepartment of Mathematics and Computer Science, Montclair State University, Montclair, NJ 07043, USA
Abstract:
The pressure drop in a horizontal rotating fluidized bed was measured using slotted and sintered metal cylindrical gas distributors as a function of rotating speed, gas velocity and bed thickness. Experiments were conducted using polydisperse alumina particles and nearly monodisperse glass beads. The pressure drop for the slotted distributor exhibited a much larger pressure overshoot at incipient fluidization than the sintered metal distributor. This behavior was also studied using high-resolution photography. Physically consistent explanations are presented for the observed phenomena. The experimental results are compared to theoretical models available in the literature.