In this work, we develop a distributed-parameter model which is capabl
e of predicting the dynamic response of bed height as a function of th
e salient properties of the solid and fluid phases. We show that a mod
el which captures both the convective and dispersive nature of solid t
ransport in a solid-liquid fluidized bed can adequately predict the be
d-height evolution under both step increases and step decreases in the
fluidization velocity. The convective term is described by an augment
ed form of the Richardson-Zaki expression. We propose a novel Bingham-
like model to describe the diffusive characteristics of the solid-liqu
id system. It is shown that the dispersion scales as a function of the
dimensionless column-average solid velocity, which is proportional to
a yield stress. When this velocity is large, as in the initial period
after a step change, the dispersion mechanism is not operable in the
system. After the column-average solid velocity drops below a critical
level, the dispersion mode is operable. A series of experiments were
performed for both step increases and step decreases in the fluidizati
on velocity. Model predictions for the bed-height transients are in go
od agreement with experimental data. (C) 1997 Elsevier Science Ltd.