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Flow and Transfer

Mass Transfer Performance of Layered Packing Cross-flow Rotating Packed Bed

  • GAO Ya-Jie ,
  • YUAN Zhi-Guo ,
  • LIU You-Zhi ,
  • LIU Hui-Jun ,
  • DU Jie ,
  • LIANG Peng-Fei
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  • 1. Shanxi Province Key Laboratory of Higee-Oriented Chemical Engineering
    2. Research Center of Shanxi Province for High Gravity Chemical Engineering and Technology
    3. Research Center of Shanxi Province for High Gravity Chemical Engineering and Technology, North University of China, Shanxi Province Key Laboratory of Higee-Oriented Chemical Engineering, Taiyuan

Received date: 2016-07-12

  Revised date: 2016-08-31

  Online published: 2017-02-22

Abstract

In order to verify the intensification effect of LPC?RPB (Layered Packing Cross-flow Rotating Packed Bed) on gas-side mass transfer, optimize the device structure and improve the mass transfer efficiency, the gas-film limited system of the absorption process of SO2 by NaOH solution was applied in this work. The influence of high gravity factor β, empty bed gas velocity u and liquid spray density q on volumetric gas-phase mass transfer coefficients (kyae) and the intensification effect were investigated. The results indicated that the kyae values increased with the increase of β, u and q. Under the conditions of β=55, u=1.53 m/s and q=3 m3/(m2?h), kyae can reach 28 s?1, which is 10~75 times higher than the spray column and 1.4~2.2 times than the traditional cross-flow rotating packed bed. Besides, with the characteristics of milder operating conditions, simpler structure and lower energy consumption compared to SP?RPB (Split Packing Rotating Packed Bed), LPC?RPB showed a good performance of effectively intensifying the gas-film controlled mass transfer process.

Cite this article

GAO Ya-Jie , YUAN Zhi-Guo , LIU You-Zhi , LIU Hui-Jun , DU Jie , LIANG Peng-Fei . Mass Transfer Performance of Layered Packing Cross-flow Rotating Packed Bed[J]. The Chinese Journal of Process Engineering, 2017 , 17(1) : 47 -51 . DOI: 10.12034/j.issn.1009-606X.216234

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