A systematic procedure is developed for designing an integrated crystalliza
tion system by considering the interaction between crystallization and down
stream processing. Potential problems related to unit operations such as fi
ltration, washing, dewatering, recrystallization, and drying are anticipate
d and resolved by determining an operating policy and configuration for the
crystallizer as well as the downstream units. The approach can be applied
to both batch and continuous crystallizers. First, the possible impacts of
particle-size distribution (PSD) on the downstream processing units are ide
ntified. This forms the basis for determining a target PSD in the second st
ep. Third, possible means by which the desired PSD can be achieved are sele
cted. Fourth, the alternatives thus generated are evaluated and compared to
identify, the best design. Heuristics are provided along the way to guide
the decision making. Shortcut equipment models are used to compare the perf
ormance of the alternatives. The procedure is illustrated with two industri
al examples, including the production of adipic acid.