Extractive fermentation for improved production and recovery of lipase derived from Burkholderia cepacia using a thermoseparating polymer in aqueous two-phase systems

An extractive fermentation technique was developed using a thermoseparating reagent to form a two-phase system for simultaneous cell cultivation and downstream processing of extracellular Burkholderia cepacia lipase. A 10% (w/w) solution of ethylene oxide-propylene oxide (EOPO) with a molecular mass of 3900. g/mol and pH 8.5, a 200. rpm speed, and 30 °C were selected as the optimal conditions for lipase production (55. U/ml). Repetitive batch fermentation was performed by continuous replacement of the top phase every 24. h, which resulted in an average cell growth mass of 4.7. g/L for 10 extractive batches over 240. h. In scaling-up the process, a bench-scale bioreactor was tested under the conditions that had been optimized in flasks. The production rate and recovery yield were higher in the bioreactor compared to fermentation performed in flasks.