The crystallization of the two polymorphs of l-glutamic
acid (LGA) is carried out in a continuous crystallization process,
and its performance according to different criteria is evaluated.
The study aims at identifying suitable operating conditions for producing
either αLGA or βLGA with a high polymorphic purity. To
this end, we investigate the process both from a theoretical perspective
and through experiments using either a single stirred-tank crystallizer
or a cascade of two stirred-tank crystallizers in series. In terms
of theory, we extend the MSMPR-based steady-state stability analysis
of Farmer et al. (AIChE J.20166235053514) by accounting
for the possibility of a nonrepresentative withdrawal of the solid
phase from the crystallizer. Additionally, the process is simulated
using population balance equations, thereby investigating the effect
of operating conditions on polymorphic purity, yield, and productivity.
Guided by the model-based conclusions, we identified suitable operating
conditions and experimentally tested them. The experimental campaign
has demonstrated that βLGA could be successfully and continuously
produced in both process configurations according to the theory with
performance as expected, whereas that was not possible for αLGA.
The difference between the two stems from different operational challenges,
whose consequence is that steady-state operation is attained in the
case of βLGA but not in that of αLGA. In the former case,
the needle-like βLGA crystals, which exhibit no agglomeration,
tend to be only slightly oversampled; in the latter case, the prismatic
αLGA crystals undergo major agglomeration and hence are very
difficult to suspend and effectively withdraw from the crystallizer.