The design and modelling of crystallisation processes without recourse to e
xperimental results is still very difficult since nucleation, attrition, ag
glomeration, and growth all influence one another and largely determine the
product properties. Nevertheless, simplified models exist for all partial
steps. These can predict the mechanism predominating at given supersaturati
on for a range of sub stances. The models presented permit calculation of t
he rate-determining kinetics over a wide range or, given a knowledge of the
metastable range, permit prediction of a maximum rate of agglomeration, nu
cleation, and growth. This can be considered in estimation of the expected
particle sizes. Based on the kinetics and giving due consideration to the d
emonstrated mutual interactions, the order of magnitude of important operat
ing parameters for desired product properties, such as the optimum supersat
uration, can be determined.