A dynamic model of the liquid fluidized bed containing two or more sol
id particle species of different size and density is presented. The mo
del incorporates the particle mass transport mechanisms of the convect
ion and the dispersion. The movement of the upper interface of the bed
subject to a change in the liquid velocity is specified using the mas
s balance constraint. The particle velocities and dispersion coefficie
nts are evaluated using correlations. The model is capable of describi
ng the bed expansion, concentration profiles of the individual particl
e species, the bulk density profile, and the occurrence of layer inver
sion.