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Micromixing in a rotating packed bed

  • Yu Shao Chen
  • , Hwai Shen Liu*
  • , Chia Chang Lin
  • , Wen Tzong Liu
  • *Corresponding author for this work
  • National Taiwan University
  • Industrial Technology Research Institute of Taiwan

Research output: Contribution to journal › Journal Article › peer-review

53 Scopus citations

Abstract

A parallel-competing chemical test reaction was performed in a Higee liquid/liquid system to evaluate the micromixing efficiency. According to the experimental results, it indicated that increasing rotational speed and liquid flow rate could intensify micromixing effectively. The micromixing efficiency in a Higee system was shown to be higher than other reported types of mixing devices, and the centrifugal force was also effective in enhancing micromixing when the liquid viscosity increased. An empirical correlation was then obtained, implying that the characteristic mixing time was proportional to the rotational speed to the power of -0.64. To investigate the relation between micromixing and mass transfer, an experiment of deoxygenation was performed. It is found that mass transfer resistance decreased as the micromixing efficiency increased.

Original languageEnglish
Pages (from-to)1122-1128
Number of pages7
JournalJournal of Chemical Engineering of Japan
Volume37
Issue number9
DOIs
StatePublished - 09 2004
Externally publishedYes

Keywords

  • Mass transfer
  • Micromixing
  • Rotating packed bed
  • Segregation index
  • Viscous media

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