The importance of spatial variations of the conditions in industrial-s
cale, agitated batch cooling crystallizers is investigated by computer
simulations. A three-compartment model is developed considering prima
ry and magma density-dependent secondary nucleation. An increasing cry
stallizer size is described by an increasing suspension turnover time.
It is shown that accumulation of larger crystals in the bottom region
, localized supersaturation generation and variations in the secondary
nucleation rate due to varying local mixing intensity will, under nor
mal conditions, exert a low and often negligible influence on the prod
uct-size distribution of an industrial unit. In a batch process, the p
roduct-size distribution is governed mainly by the conditions early in
the process. During this period the supersaturation half-life is much
longer than the suspension turnover time, and the influence of local
variations becomes weak.