This study is to clarify the flow characteristics and hold up behavior
of powders in a packed bed with lateral inlets through which gas and
powders are injected. The experiments were carried out for two kinds o
f the packed particles and powders. Longitudinal and radial distributi
ons of powder hold up as well as longitudinal distribution of pressure
in the packed bed were measured. It was found that more powders depos
ited in the lower part, especially in the lower central part of the pa
cked bed and that the total hold up of powders increased with the incr
ease in the diameter of the packed particles. No blockade occurred for
powders of 98 and 175 mum under the experimental conditions. The gas
and powder two-phase flow in the packed bed was simulated by a two-dim
ensional mathematical model considering gravitational force, the inter
action forces between gas and the packed particles, gas and powders, a
nd powders and the packed particles. The effect of static hold up of p
owders on the voidage of the packed bed was reflected in computations
through the trial and error approach according to the experimental dat
a of total hold up of powders. The pressure distribution computed by t
he mathematical model has good agreement with the observed one, and so
that the static and dynamic hold ups of powders obtained are reasonab
le.