(422f) Continuous Simultaneous Hydrogenation and Acetylation of 4-Nitrophenol to Paracetamol
AIChE Annual Meeting
2024
2024 AIChE Annual Meeting
Pharmaceutical Discovery, Development and Manufacturing Forum
Continuous Process: Next Generation Advancements
Tuesday, October 29, 2024 - 5:15pm to 5:36pm
Traditional hydrogenation methods operate using pressurized stirred tank batch reactors. The high temperature, pressure, and solvent loading of these processes introduce safety issues as well as poor Green Chemistry metrics. Continuous hydrogenation has been shown to mitigate the explosive risks of hydrogenation in industrial processes through reducing required hydrogen headspace and has additional advantages of consistent product quality and superior Green Chemistry metrics.
Careful design of the reaction conditions is required to achieve high selectivity, as the key intermediate of the hydrogenation reaction, 4-aminophenol, is highly reactive and undergoes various side reactions. In previous work, we showed that simultaneous hydrogenation and acetylation of 4-aminophenol in one vessel was highly effective for improving selectivity in a fed-batch mechanochemical reactor. Importantly, careful control of the rate of fed batch acetic anhydride addition was vital for maximizing selectivity.
Here, we implement the reaction engineering strategies learned during our design of our fed-batch mechanochemical synthesis in a flow reactor for continuous, selective paracetamol synthesis with high volumetric productivity. To our knowledge, this is one of the first continuous syntheses of paracetamol from the hydrogenation of 4-nitrophenol with elemental hydrogen.