Development and characterization of a silica monolith immobilized enzyme micro-bioreactor

Koei Kawakami, Yoshihide Sera, Shinji Sakai, Tsutomu Ono, Hiroyuki Ijima

研究成果: ジャーナルへの寄稿学術誌査読

52 被引用数 (Scopus)

抄録

Several 10-cm-long capillary tubes [made of poly(ether ether ketone) (PEEK)] with inside diameters of 0.1-2.0 mm were filled with silica monolith-immobilized protease derived by in situ sol-gel transition from a 1:4 mixture of tetramethoxysilane and methyltrimethoxysilane. Transesterification between 20 mM (S)-(-)-glycidol and 0.4 M vinyl n-butyrate in an organic solvent was used as the test reaction. The substrate solution flowed through the column at a flow rate of 0.0004-5.0 mL·min-1. The conversion in the micro-bioreactor was higher than that in the batch reactor at a high liquid flow rate. When three tubes were connected in series, the conversion at a fixed ratio of the mass of the enzyme to the liquid flow rate was increased by approximately 50%, because of the tripling of the flow rate as compared to the case with a single tube. Changes in the tube diameter had no influence on the conversion at a fixed superficial liquid velocity. Further, the conversion increased with a decrease in the enzyme content. These results were ascribed to the apparent effect of liquid-solid mass transfer and were analyzed quantitatively using a simple mathematical model.

本文言語英語
ページ(範囲)236-240
ページ数5
ジャーナルIndustrial and Engineering Chemistry Research
44
1
DOI
出版ステータス出版済み - 1月 5 2005

!!!All Science Journal Classification (ASJC) codes

  • 化学一般
  • 化学工学一般
  • 産業および生産工学

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