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author:

Huang, G.-Q. (Huang, G.-Q..) [1] | Jin, Q. (Jin, Q..) [2] | Wang, H.-X. (Wang, H.-X..) [3]

Indexed by:

Scopus PKU CSCD

Abstract:

The indirect sequence as a conventional process was simulated by using Aspen Plus software for the separation of thionyl chloride. And divided wall column (DWC) was proposed as an innovative process to separate thionyl chloride. Furthermore, the effect of feed stage, side draw stage, the ratio of reflux rate to feed and distribution ratio on the product purity and reboiler duty was discussed. The optimum operating conditions determined are as follows: the feed stage is the 6th tray of pre-fractionator, the side draw stage is the 55th tray of main column, the ratio of reflux rate to feed is 4.45, the liquid distribution ratio is 1.60, and the vapor distribution ratio is 1.98. The results show that DWC operated in optimal conditions can save condenser duty and reboiler duty by 34.62% and 34.64% respectively, compared with the conventional indirect sequence. Meanwhile, DWC can save capital cost by 17.27% from the calculating result of CAPCOST software. So DWC for the separation of thionyl chloride is an energy saving and efficient separation technology.

Keyword:

Divided wall column; Energy saving; Simulation; Thionyl chloride

Community:

  • [ 1 ] [Huang, G.-Q.]School of Chemical Engineering and Technology, Tianjin University, Tianjin 300072, China
  • [ 2 ] [Jin, Q.]School of Chemical Engineering and Technology, Tianjin University, Tianjin 300072, China
  • [ 3 ] [Wang, H.-X.]College of Chemical Engineering, Fuzhou University, Fuzhou 350007, Fujian Province, China

Reprint 's Address:

  • [Jin, Q.]School of Chemical Engineering and Technology, Tianjin University, Tianjin 300072, China

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Source :

Chemical Engineering (China)

ISSN: 1005-9954

Year: 2014

Issue: 3

Volume: 42

Page: 18-23

Cited Count:

WoS CC Cited Count:

SCOPUS Cited Count:

ESI Highly Cited Papers on the List: 0 Unfold All

WanFang Cited Count:

Chinese Cited Count:

30 Days PV: 1

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