A new fluidization regime, the circulating fluidization regime, is ide
ntified for the upwards liquid-solid fluidization operation. This circ
ulating fluidization regime is characterized by non-uniform radial dis
tribution of liquid velocity, particle velocity and particle hold-up i
n the bed, different from the conventional fluidization regime and the
transport regime where the radial flow structure is more uniform. Bec
ause of the radial non-uniform flow structure, the flow behaviours in
the circulating fluidization regime cannot be predicted with the empir
ical relationships based upon homogeneous fluidization.