In this work, both direct design approaches were implemented to investigate the impact on the particle shape, length, and filtration time of needle shaped particles. Preliminary results have indicated significant improvement in the overall crystallization-filtration process performance. Using an alternative turbidity-based DNC-based direct design approach, the filtration time was reduced by a factor of four compared to the standard recipe. The improved procedure not only reduces the unit operation cycle times, but also improves the particle shape for better downstream operations (i.e. drying, transport). The analysis of the product crystals using High Performance Liquid Chromatography (HPLC) indicates that the impurity profile of the agrochemical compound was not compromised with the thermocycles. The QbC-based direct design approaches were also evaluated in larger scale (5 L) crystallization systems indicating that the feedback control based rapid design approach can lead to fast and robust scale-up of agrochemical crystallization processes.
References:
(1) Bondi, R. W.; Drennen, J. K. Quality by Design and the Importance of PAT in QbD; Academic Press, 2011; Vol. 10.
(2) Su, Q.; Ganesh, S.; Moreno, M.; Bommireddy, Y.; Gonzalez, M.; Reklaitis, G. V.; Nagy, Z. K. A Perspective on Quality-by-Control (QbC) in Pharmaceutical Continuous Manufacturing. Comput. Chem. Eng. 2019, 125, 216–231.
(3) Bakar, M. R. A.; Nagy, Z. K.; Saleemi, A. N.; Rielly, C. D. The Impact of Direct Nucleation Control on Crystal Size Distribution in Pharmaceutical Crystallization Processes. Cryst. Growth Des. 2009, 9 (3), 1378–1384.
(4) Saleemi, A. N.; Rielly, C. D.; Nagy, Z. K. Comparative Investigation of Supersaturation and Automated Direct Nucleation Control of Crystal Size Distributions Using ATR-UV/Vis Spectroscopy and FBRM. Cryst. Growth Des. 2012, 12 (4), 1792–1807.