Gas- liquid- solid inverse fluidized bed were studied in which the gas
and the continuous liquid phase flow countercurrently fluidizing part
icles that are lighter than the liquid. Conductivity and static pressu
re measurements were combined to provide the vertical profiles of the
gas liquid and solid holdup, in beds of 4- or 6-mm polypropylene parti
cles with a density of about 870 kg/m(3). Various bed heights were obt
ained with different measurement methods. The minimum fluidization vel
ocity was estimated using the bed static pressure gradient. A new tran
sition velocity, called the uniform fluidization velocity, was identif
ied using conductivity measurements. This is the superficial liquid ve
locity at which the fluidization quality becomes the same throughout t
he bed.