2025 AIChE Annual Meeting
(157a) Advancing Biopharmaceutical Manufacturing: Continuous Crystallization of Therapeutic Full-Length Monoclonal Antibodies
Authors
Crystallization processes for biomacromolecules are much less mature compared to small molecules due to their size, complexity, and dynamic behavior, which constitutes a challenge for the biopharmaceutical industry. For this reason, the first processes being employed were batch processes. Nowadays, these processes are relatively well-established and still the predominant technology. Batch-to-continuous transition of biopharmaceutical production has been continuously advancing and applied during the last decade to improve product quality attributes at a low manufacturing cost [3]. However, only a few studies have reported experimental methodologies to continuously crystallize biomolecules (i.e., model proteins: lysozyme, insulin).
This study highlights, to the best of our knowledge, the first integrated crystallization-based platform to crystallize full-length mAbs. The experimental apparatus comprises a series of three mixed suspension mixed product removal crystallizers (MSMPRCs) with a pressure-driven slurry transfer [4]. In addition, the MSMPRCs are equipped with process analytical technology (PAT) probes for real-time monitoring of different mAb crystallization processes, including in-line crystal size distribution (CSD), microscopy, and Raman spectroscopy. Complementary, off-line sampling consists of e.g., microscopy imaging and mAb concentration measurement (HPLC) to assess the quality and efficacy of the continuous crystallization process. Ultimately, needle-shaped crystals are produced and characterized using SAXS and Cryo-EM to ensure they are mAb crystals. Lastly, AI-based image analysis is implemented to obtain CSD over time, and mAb crystallization kinetics are quantified by Population Balance Modeling and considering a steady-state MSMPR model.
References
[1] M. Hong et al., Computers & Chemical Engineering, 2018, 110, 106–114.
[2] A. Shukla et al., Journal of Chromatography B, 2007, 848, 28–39.
[3] M. Sun Hong et al., American Pharmaceutical Review, 2020, 1–4.
[4] Y. Cui et al., Organic Process Research & Development, 2016, 20, 1276–1282.
Acknowledgements
This work was funded by FDA under the contract number 75F40121C00111.