Solid-state deracemization
via temperature cycles converts a racemic
crystal mixture into an enantiopure product by periodic cycling of
the temperature in the presence of a racemization catalyst. A continuous
counterpart of this conventional batch-operated process is proposed
that can be performed in mixed suspension mixed product removal crystallizers
(MSMPRCs). More specifically, three different configurations are described
to perform periodic forcing via temperature cycles, which differ from
each other in the type of the feed and in the withdrawal system. We
have developed a model by extending our recent population balance
equation model of batch solid-state deracemization via temperature
cycles, and we exploit this tool to analyze the start-up and periodic
steady-state behavior. Moreover, we compare the performance of the
different configurations based on the selected key performance indicators,
namely, average periodic steady-state enantiomeric excess and productivity.
The process with solution feed yields pure enantiomers, while the
solid and suspension-fed process alternatives result in highly enantiomerically
enriched crystals. We further design an MSMPRC cascade to overcome
this purity limitation. This work discusses guidelines on how to transform
the batch process of temperature cycles into a continuous operation,
which enables stable, unattended operation and chiral crystal production
with consistent product quality.