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author:

Zhang, W. (Zhang, W..) [1] | Xie, P. (Xie, P..) [2] | Li, Y. (Li, Y..) [3] | Teng, L. (Teng, L..) [4] | Zhu, J. (Zhu, J..) [5]

Indexed by:

Scopus

Abstract:

Rotating packed bed (RPB) has been widely noted for its good mass transfer performance and tangible size savings, and its advantages are especially obvious in space-intensive scenarios, such as purification of natural gas on offshore platforms. Liquid maldistribution in RPBs has a serious impact on mass transfer performance. However, it is difficult to accurately obtain and predict the liquid flow characteristics and liquid distribution in RPBs by experimental methods. Therefore, the liquid flow characteristics and liquid distribution analysis of multi-nozzle RPBs based on computational fluid dynamics (CFD) models is performed in this paper. The simulation results indicate that increasing of the number of nozzles and nozzle width at two different rotational speeds increases the liquid holdup and decreases the degree of liquid dispersion. In addition, a liquid maldistribution index within RPBs is proposed and investigated. The circumferential distribution of the liquid becomes uniform as the number of nozzles increase, but the uniformity gets worse as the width of nozzle increases, under the same total liquid flow rate. The more the number of nozzles, the more uniform the overall liquid distribution; on the contrary, the larger the nozzle width, the more uneven the overall liquid distribution. © 2020 Elsevier B.V.

Keyword:

Computational fluid dynamics; Hydrodynamic characteristics; Liquid distribution; Nozzle; Rotating packed bed

Community:

  • [ 1 ] [Zhang, W.]College of Pipeline and Civil Engineering, China University of Petroleum (East China), Qingdao, 266580, China
  • [ 2 ] [Zhang, W.]Shandong Provincial Key Laboratory of Oil & Gas Storage and Transportation Security, China University of Petroleum (East China), Qingdao, 266580, China
  • [ 3 ] [Xie, P.]Global Energy Interconnection Research Institute Europe GmbH, Berlin, 10623, Germany
  • [ 4 ] [Li, Y.]College of Pipeline and Civil Engineering, China University of Petroleum (East China), Qingdao, 266580, China
  • [ 5 ] [Li, Y.]Shandong Provincial Key Laboratory of Oil & Gas Storage and Transportation Security, China University of Petroleum (East China), Qingdao, 266580, China
  • [ 6 ] [Teng, L.]Department of Chemical Engineering, Fuzhou University, Fuzhou, 350108, China
  • [ 7 ] [Zhu, J.]College of Pipeline and Civil Engineering, China University of Petroleum (East China), Qingdao, 266580, China
  • [ 8 ] [Zhu, J.]Shandong Provincial Key Laboratory of Oil & Gas Storage and Transportation Security, China University of Petroleum (East China), Qingdao, 266580, China

Reprint 's Address:

  • [Xie, P.]Global Energy Interconnection Research Institute Europe GmbH, College of Pipeline and Civil Engineering, China University of Petroleum (East China)Germany

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Source :

Chemical Engineering and Processing - Process Intensification

ISSN: 0255-2701

Year: 2020

Volume: 158

4 . 2 3 7

JCR@2020

3 . 8 0 0

JCR@2023

ESI HC Threshold:132

JCR Journal Grade:2

CAS Journal Grade:3

Cited Count:

WoS CC Cited Count:

SCOPUS Cited Count: 35

ESI Highly Cited Papers on the List: 0 Unfold All

WanFang Cited Count:

Chinese Cited Count:

30 Days PV: 2

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