PAT-based design of agrochemical co-crystallization processes: a case-study for the selective crystallization of 1:1 and 3:2 co-crystals of p-toluenesulfonamide/triphenylphosphine oxide
posted on 2016-07-04, 10:38authored byKeddon Powell, D.M. Croker, Chris Rielly, Zoltan NagyZoltan Nagy
In this study, the selective crystallization and characterization of the stoichiometric forms of the p-toluenesulfonamide/triphenylphosphine oxide (p-TSA-TPPO) co-crystal system in acetonitrile (MeCN) is demonstrated using batch and semi-batch crystallizers. In the batch study, both 1:1 and 3:2 p-TSA-TPPO were successfully isolated as pure forms. However, process variability was observed in a few experimental runs. To address the batch process variability issue, a control strategy was implemented using temperature cycling, aided by in situ process analytical technologies (PAT) to convert from 3:2 to 1:1 p-TSA-TPPO. In the semi-batch co-crystallization studies, the two molecular co-formers, p-TSA and TPPO, were dissolved in MeCN and pumped separately to the crystallizer. Changing the flow rates of the respective active ingredients allowed control over the co-crystallization outcome, and presents as a promising opportunity for development of a continuous co-crystallization process.
History
School
Aeronautical, Automotive, Chemical and Materials Engineering
Department
Aeronautical and Automotive Engineering
Published in
Chemical Engineering Science
Volume
152
Pages
95 - 108
Citation
POWELL, K.A. ... et al, 2016. PAT-based design of agrochemical co-crystallization processes: a case-study for the selective crystallization of 1:1 and 3:2 co-crystals of p-toluenesulfonamide/triphenylphosphine oxide. Chemical Engineering Science, 152, pp.95-108
This work is made available according to the conditions of the Creative Commons Attribution-NonCommercial-NoDerivatives 4.0 International (CC BY-NC-ND 4.0) licence. Full details of this licence are available at: https://creativecommons.org/licenses/by-nc-nd/4.0/
Publication date
2016
Notes
This paper was accepted for publication in the journal Chemical Engineering Science and the definitive published version is available at http://dx.doi.org/10.1016/j.ces.2016.06.005