کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
4752072 | 1415989 | 2017 | 10 صفحه PDF | دانلود رایگان |

- The ospCSTR enables high selectivity, catalytic productivity and space-time yield.
- Operation periods up to 17Â d could be performed.
- Constant space-time yield was maintained over 100Â h with intermittent lipase dosing.
- Intermittent lipase dosing almost tripled catalytic productivity to 282Â gPOÂ gâ1CalB.
- Longest operation of chemo-enzymatic epoxidation reported so far.
The aim of this work was to develop a new process strategy for the in-situ lipase-mediated synthesis of α-pinene oxide. To minimize the limitation of enzyme deactivation encountered in these reaction cascades, an organic-single-phase continuous stirred tank reactor (ospCSTR) process was developed. Considering the numerous degrees of freedom of this continuous multistep reaction which due to enzyme deactivation additionally has no steady-state, the process development is a challenging task. Therefore, the influence of operating parameters on the efficiency was studied in detail. Due to the avoidance of harsh conditions, at optimized parameters α-pinene oxide was produced selectively (95%), and with high space-time yields (880 gPO Lâ1 dâ1). The catalytic productivity (118 gPO gâ1CalB) was significantly higher than previously reported. To counterbalance the reduced but still present deactivation, the opsCSTR was enhanced with intermittent enzyme dosing which, for the first time, enabled long-term operation, high catalytic productivity, and high space-time yield. With the ospCSTR augmented by enzyme dosing, we report an economical process for a chemo-enzymatic epoxidation of sensitive terpenes like e.g., α-pinene.
156
Journal: Biochemical Engineering Journal - Volume 126, 15 October 2017, Pages 68-77