Enhancing reaction selectivity by intentional control of concentration profile in catalytic microreactor

Shinji Kudo, Taisuke Maki, Hiroyuki Kono, Maria Olea, Kazuhiro Mae

研究成果: ジャーナルへの寄稿学術誌査読

1 被引用数 (Scopus)

抄録

This paper reports the results of a computational fluid dynamics (CFD) simulation for a sequential heterogeneous catalytic reaction by comparing the reaction selectivity in a catalytic microreactor with that in a conventional catalytic packed-bed reactor. The comparative simulation revealed that the catalytic microreactor has an advantage over the conventional reactor in the diffusion control regime, and that the control of concentration distribution of reactants by molecular diffusion in the microspace can enhance the selectivity of the desired product. The concentration distribution was intentionally controlled by the shape of the microreactor. The yield of the desired product in the microreactor was 1.16 times that in the packed-bed reactor. CFD simulation of methanol decomposition was also performed by fitting the parameters with the experimental results. The results of the CFD simulation verified the advantage of the microreactor.

本文言語英語
ページ(範囲)63-69
ページ数7
ジャーナルJournal of Chemical Engineering of Japan
43
1 SUPPL.
DOI
出版ステータス出版済み - 2月 5 2010
外部発表はい

!!!All Science Journal Classification (ASJC) codes

  • 化学 (全般)
  • 化学工学(全般)

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