Chen, Robbie, Couming, Vincent, Guzowski, John, Irdam, Erwin, Kiesman, William F., Kwok, Daw-Iong Albert, Liang, Wenli, Mack, Tamera, O’Brien, Erin M., Opalka, Suzanne M., Patience, Daniel, Sahli, Stefan, Walker, Donald G., Osei-Yeboah, Frederick, Gu, Chaozhan, Zhang, Xin, Stöckli, Markus, Stucki, Thiemo, Matzinger, Hanspeter, Kuhn, Roman, Thut, Michael, Grohmann, Markus, Haefner, Benjamin, Lotz, Joerg, Nonnenmacher, Michael, and Cerea, Paolangelo
As vixotrigine (1) entered a later clinical phase for trigeminal neuralgia (Zakrzewska, J. M.; et al. Lancet Neurol.2017, 16, 291−300), the development of a sustainable late-stage process was required to meet the supply needs for formulation optimization, phase 3 clinical trials, and registration stability batches (this is the expected commercial formulation). In this article, we describe how the process was streamlined from the early supply route (Giblin, G.; et al. Org. Process Res. Dev.2020, DOI: 10.1021/acs.oprd.0c00382) and a comprehensive control strategy was established. Process improvements included improving safety and scalability for a temperature-sensitive Grignard reaction, simplifying unit operations, removal of heterogenous conditions, and route redesign to afford a high yielding, one-pot sequential alkylation and amidation. Improvement in the salt formation step, combined with wet milling, resulted in improved particle properties with enhanced flow properties of the final active pharmaceutical ingredient. The process mass intensity was improved 65% while maintaining drug substance purity at more than 99.8%. This new process has been scaled up to generate metric ton quantities of drug substance.