In the pharmaceutical industries, the requirements of rapid process development and scalable design have made the tubular crystallizer a promising platform for continuous manufacturing and crystallization processes, capable of replacing conventional capital- and labor-intensive batch operations. This paper takes a process systems engineering (PSE) approach to the optimal design of a continuous antisolvent addition crystallizer to deliver the most promising product qualities, such as the crystal size distribution. A multisegment multiaddition plug-flow crystallizer (MSMA-PFC) is considered as an example of a continuous antisolvent crystallization process, in which the total number, location, and distribution of antisolvent additions are to be optimized. First-principles dynamic and steady-state mathematical models for the MSMA-PFC are presented, based on example kinetic models for nucleation and growth of paracetamol crystallizing in acetone, with water as the antisolvent. The performances of different crystallizer configurations operated under optimal design conditions are then compared. The configuration in which antisolvent could be added at a variety of different locations along the tube length and at optimal flow rates was able to outperform previous designs in the literature which considered equally spaced antisolvent additions. The use of dynamic models to detect problems during startup of an MSMA-PFC was also highlighted.

• Loughborough University

• Modeling

1. Mathematical modelling
2. modeling
3. paracetamol
4. Plug flow crystallizer
5. process system engineering
6. Research Article
7. tubular crystallizer