4.8 Article

Rapid synthesis of propyl caffeate in ionic liquid using a packed bed enzyme microreactor under continuous-flow conditions

期刊

BIORESOURCE TECHNOLOGY
卷 149, 期 -, 页码 367-374

出版社

ELSEVIER SCI LTD
DOI: 10.1016/j.biortech.2013.09.098

关键词

Biocatalysis; Continuous-flow condition; Packed bed enzyme microreactor; Propyl caffeate; Transesterification

资金

  1. China Postdoctoral Science Foundation Funded Projects [2012M510124, 2013T60505]
  2. Natural Science Foundation of China [21206061]
  3. Postdoctoral Science Foundation Funded Project of Jiangsu University [1143002085]
  4. Qing Lan Project of Jiangsu Province
  5. Graduate Innovation Project of Jiangsu Province [2012JSSPITP1482]
  6. Start Project for Introduced Talent at Jiangsu University of Science and Technology [35211002]

向作者/读者索取更多资源

Propyl caffeate has the highest antioxidant activity among caffeic acid alkyl esters, but its industrial production via enzymatic transesterification in batch reactors is hindered by a long reaction time (24 h). To develop a rapid process for the production of propyl caffeate in high yield, a continuous-flow microreactor composed of a two-piece PDMS in a sandwich-like microchannel structure was designed for the transesterification of methyl caffeate and 1-propanol catalyzed by Novozym 435 in [Bmim][CF3SO3]. The maximum yield (99.5%) in the microreactor was achieved in a short period of time (2.5 h) with a flow rate of 2 mu L/min, which kinetic constant K-m was 16 times lower than that of a batch reactor. The results indicated that the use of a continuous-flow packed bed enzyme microreactor is an efficient method of producing propyl caffeate with an overall yield of 84.0%. (C) 2013 Elsevier Ltd. All rights reserved.

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