Search

Sphingomonas sp. HXN-200 bacteria were immobilized onto gelatin and poly(3-hydroxybutyrate-co-3-hydroxyvalerate) (PHBV) microspheres in an aqueous system for industrial scale biohydroxylation. Scanning electron microscopy and confocal laser scanning microscopy were used to confirm the bacterial immobilization. The gelatin microsphere-immobilized cells successfully transformed N-benzyloxycarbonyl-pyrrolidine and N-tert-butoxycarbonyl-pyrrolidine into R-N-benzyloxycarbonyl-3-hydroxypyrrolidine and R-N-tert-butoxycarbonyl-3-pyrrolidinol at various substrate concentrations showing an improved conversion yield and product efficiency with respect to the freely suspended cells system at each reaction interval time. Additionally, in the immobilized cells system, it showed a faster reaction rate as compared to the freely suspended cells system for reaching the same product concentration. The inhibition effect due to substrate and product concentrations was significantly lower after immobilizing the bacteria onto the microspheres, which is beneficial for continuous reaction. The efficient whole-cell biocatalytic process was feasibly conducted in a 500mL preparative scale bioreactor and the conversion yield of N-benzyloxycarbonyl-pyrrolidine did not decrease after consecutive repeated use, suggesting that the microsphere-cells immobilization system was stable and reusable., (Copyright © 2014 Elsevier B.V. All rights reserved.)

A three-phase fluidized bed reactor (TPFBR) was designed to evaluate the potential of CoQ(10) production by gel-entrapped Sphingomonas sp. ZUTE03 via a conversion-extract coupled process. In the reactor, the CoQ(10) yield reached 46.99 mg/L after 8 h of conversion; a high-level yield of about 45 mg/L was maintained even after 15 repetitions (8 h/batch). To fully utilize the residual precursor (para-hydroxybenzoic acid, PHB) in the aqueous phase, the organic phase was replaced with new solution containing 70 mg/L solanesol for each 8 h batch. The CoQ(10) yield of each batch was maintained at a level of about 43 mg/L until the PHB ran out. When solid solanesol was fed to the organic phase for every 8 h batch, CoQ(10) could accumulate and reach a yield of 171.52 mg/L. When solid solanesol and PHB were fed to the conversion system after every 8 h batch, the CoQ(10) yield reached 441.65 mg/L in the organic phase after 20 repetitions, suggesting that the conversion-extract coupled process could enhance CoQ(10) production in the TPFBR., (Copyright © 2011 Elsevier Inc. All rights reserved.)