In one of the two penultimate steps in the commercial
route to
nemtabrutinib, a ketone intermediate is formed from 7-bromo-6-chloro-7-deazapurine
and methyl 2-chloro-4-phenoxybenzoate in a series of reactions mediated
by methyllithium and n-butyllithium. Flow chemistry
was identified in development as a useful tool for safe and efficient
scale-up for two of these reactions while minimizing the formation
of unwanted impurities. Here, we present the first pilot-scale implementation
of the process where a tubular flow reactor was employed to produce
multiple kilograms of the ketone intermediate. Practical considerations
for large-scale operations are discussed, including operation at low
temperatures around −30 °C, stable and consistent control
of flow rates, and planning for the prevention of and recovery from
upset scenarios. Careful design and construction of equipment and
procedures allowed for the successful execution of five pilot-scale
batches with consistent yield and product quality to produce material
needed for clinical development. Across the campaign, average isolated
yield for the process was approximately 65%, with an average purity
of 99.9% by weight. Also presented are the findings from a series
of large-scale flow experiments, where temperature, residence time,
and reaction stoichiometry were simultaneously varied to assess process
robustness. In these experiments, n-butyllithium
stoichiometry was found to have the greatest impact on reaction yield,
as measured by product LC area percent. Additionally, the process
impurities studied were each sensitive to a different combination
of the varied parameters. Learnings from this pilot campaign were
critical to guide future development efforts en route to a potential
commercial supply of nemtabrutinib.