Mass Transport of Diazomethane across Teflon AF2400 Membrane for Scale-Up Development

Diazomethane is an attractive C1 building block in organic chemistry, but its hazardous nature presents scale-up challenges to this date. The use of a Teflon AF2400 membrane, most commonly in a tube-in-tube reactor setup, is the current state-of-the-art methodology for inherently safer laboratory-scale generation, separation, and consumption of anhydrous diazomethane. For the successful scale-up of this membrane process, the key mass transfer coefficient of the AF2400 membrane, its permeability for diazomethane, was investigated. We report in this contribution a novel methodology to determine diazomethane permeability for the rational scale-up of membrane processes for the safe handling of diazomethane. Missing physical properties of diazomethane were established, and the full mass balance of in situ-generated diazomethane within the tube-in-tube reactor was experimentally validated. A numerical model of the membrane reactor system in combination with experimental data yielded a permeability value of 414 barrer. This result enables scale-up development of the laboratory membrane reactor toward production-scale systems.