Biotechnology and Bioengineering · 2005 · 108 citations · 19 references
Life SciencesBiotechnologyChemical EngineeringBiocatalysisBioprocess EngineeringBioreactor DesignBioprocess Scale-upBioreaction EngineeringBioreactor OperationMicrobial BiocatalysisMicrobial BiotransformationMicrobial Fermentation BioreactorsBaeyer-villiger OxidationBioreactor Scale-upMicrobial Mediation Of Chemical TransformationsMicrobial OxidationOxygenationProduct Yield OptimizationProductivitySubstrate Feeding Control
This study is demonstrating the scale up of asymmetric microbial Baeyer-Villiger oxidation of racemic bicyclo[3.2.0]hept-2-en-6-one (1) to the kilogram scale using a 50 L bioreactor. The process has been optimized with respect to bottlenecks identified in downscaled experiments. A high productivity was obtained combining a resin-based in situ substrate feeding and product removal methodology (in situ SFPR), a glycerol feed control, and an improved oxygenation device (using a sintered-metal sparger). As expected both regioisomeric lactones [(-)-(1S,5R)-2 and (-)-(1R,5S)-3] were obtained in nearly enantiopure form (ee > 98%) and good yield. This represents the first example of such an asymmetric Baeyer-Villiger biooxidation reaction ever operated at that scale. This novel resin-based in situ SFPR technology therefore clearly opens the way to further (industrial) upscaling of this highly valuable (asymmetric) reaction.
19
Identification of a Baeyer–Villiger monooxygenase sequence motif
Marco W. Fraaije, Nanne M. Kamerbeek, Willem J. H. van Berkel et al. · FEBS Letters · 2002 · 221 citations · Full text
Véronique Alphand, Roland Furstoss · The Journal of Organic Chemistry · 1992 · 147 citations