Liquid-Liquid-Liquid Three Phase Extraction Apparatus:Operation Strategy and Influences on Mass Transfer Efficiency

何秀琼; 黄昆; 于品华; 张超; 谢铿; 李鹏飞; 王娟; 安震涛; 刘会洲

doi:10.1016/S1004-9541(12)60359-0

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Liquid-Liquid-Liquid Three Phase Extraction Apparatus:Operation Strategy and Influences on Mass Transfer Efficiency

Updated：2026-01-06

- Liquid-Liquid-Liquid Three Phase Extraction Apparatus:Operation Strategy and Influences on Mass Transfer Efficiency
- Liquid-Liquid-Liquid Three Phase Extraction Apparatus:Operation Strategy and Influences on Mass Transfer Efficiency
- 中国化学工程学报（英文版） 2012年20卷第1期页码：27-35
- Affiliations：
  
  1. Key Laboratory of Green Process and Engineering, Institute of Process Engineering, Chinese Academy of Sci-ences,Beijing,China,100190
  2. Graduate University of Chinese Academy of Sciences,Beijing,China,100049
- Author bio：
- Funds：
  
  Supported by the National Natural Science Foundation of China (51074150,21027004);the National Basic Research Program of China (2012CBA01203,2007CB613507);the Innovative Research Group Science Fund (20221603)
- DOI：10.1016/S1004-9541(12)60359-0
  中图分类号： TQ028.32
- 纸质出版：2012
- Accepted：
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何秀琼, 黄昆, 于品华, 等. Liquid-Liquid-Liquid Three Phase Extraction Apparatus:Operation Strategy and Influences on Mass Transfer Efficiency[J]. 中国化学工程学报（英文版）, 2012,20(1):27-35.

HE Xiuqiong, HUANG Kun, YU Pinhua, ZHANG Chao, XIE Keng, LI Pengfei, WANG Juan, AN Zhentao, LIU Huizhou. Liquid-Liquid-Liquid Three Phase Extraction Apparatus:Operation Strategy and Influences on Mass Transfer Efficiency[J]. , 2012, 20(1): 27-35.
何秀琼, 黄昆, 于品华, 等. Liquid-Liquid-Liquid Three Phase Extraction Apparatus:Operation Strategy and Influences on Mass Transfer Efficiency[J]. 中国化学工程学报（英文版）, 2012,20(1):27-35. DOI： 10.1016/S1004-9541(12)60359-0.

HE Xiuqiong, HUANG Kun, YU Pinhua, ZHANG Chao, XIE Keng, LI Pengfei, WANG Juan, AN Zhentao, LIU Huizhou. Liquid-Liquid-Liquid Three Phase Extraction Apparatus:Operation Strategy and Influences on Mass Transfer Efficiency[J]. , 2012, 20(1): 27-35. DOI： 10.1016/S1004-9541(12)60359-0.

摘要

中图分类号:

Abstract

A new mixer-settler-mixer three chamber integrated extractor is proposed in this work for liquid-liquid-liquid three phase countercurrent and continuous extraction.Experiments revealed the influences of the structural design of the three-liquid-phase extractor and some key operational parameters on three-phase partition of two phenolic isomers

-nitrophenol(

-NP) and o-nitrophenol(

-NP).The model three-liquid-phase extraction system used here is nonane(organic top-phase)-polyethylene glycol(PEG 2000)(polymer middle-phase)-(NH

)

aqueous solution(aqueous bottom-phase).It is indicated that agitating speed and retention time in three-phase mixer are key parameters to extraction fraction of nitrophenol.Dispersion band behavior is related to agitating intensity

and its occurrence does not affect the extraction fraction of target compounds.The present work highlights the possibility of a feasible approach of scaling up of the proposed three-phase extraction apparatus for future industrial-aimed applications.

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