The fluidized-bed crystallizers have long been used in the chemical industr
y and recently for water treatment as the so-called pellet reactors. This r
eport summarizes the experimental results regarding hydrodynamics and cryst
al growth rates in laboratory-scale fluidized-bed crystallizers. The two-st
ep crystal growth model rather than the over-all model is adopted to explai
n the observed kinetic behaviors. In using the two-step growth model, the d
isadvantage is the uncertainty of the surface-reaction order. A reliable me
thod is suggested to explore the surface-reaction order using a lean fluidi
zed-bed crystallizer The crystal growth process of sparingly soluble salts,
which have been studied recently for a few systems, seems more complex tha
n that of soluble salts. Then, a comparison of crystal growth kinetics of s
oluble salts is made between the dense and lean fluidized-bed crystallizers
. As a conclusion, the two-step growth model is suitable for the estimation
of crystal growth rates in the design of a liquid fluidized-bed crystalliz
er. (C) 1999 Elsevier Science B.V. All rights reserved.