In bubbling fluidized bed combustion and catalytic cracking, elutriati
on is a major cause of inefficiency, while it is highly desirable, for
instance, in sludge incineration. Whether the intention is to quench
or promote elutriation, the involved phenomena must be properly known
if the process is to be efficiently controlled. In this work, entrainm
ent and elutriation are reviewed and a modelling proposal is developed
. The main concern relates to bubbling beds of wide spread particle si
ze distributions under vigorous fluidization. The particles are subdiv
ided into three classes: critical fines, smalls and larges. Critical f
ines are particles whose terminal velocities are much lower than the g
as superficial velocity, and are assumed to be instantaneously entrain
ed at the bed surface. Smalls and larges are particles whose terminal
velocities are respectively fewer and higher than the gas superficial
velocity, and are assumed to be entrained through the bubble wake ejec
tion mechanism. The bed surface entrainment model presents parameters
which must be evaluated from empirical data. Comparison to experiment
shows that, for U/U(nf)greater than or equal to 10, f(w) xi(k) should
increase with U/U-mb and a correlation is proposed to account for this
variation. The elutriation model is based on phenomenological observa
tions from experiment, coming out with parameters which must be set fo
r specific situations.