Mass Transfer of Copper(Ⅱ) in Hollow Fiber Renewal Liquid Membrane with Different Carriers

张卫东; 崔春花; 杨彦强

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Mass Transfer of Copper(Ⅱ) in Hollow Fiber Renewal Liquid Membrane with Different Carriers

Updated：2026-01-06

- Mass Transfer of Copper(Ⅱ) in Hollow Fiber Renewal Liquid Membrane with Different Carriers
- Mass Transfer of Copper(Ⅱ) in Hollow Fiber Renewal Liquid Membrane with Different Carriers
- 中国化学工程学报（英文版） 2010年18卷第2期页码：346-350
- Affiliations：
  
  State Key Laboratory of Chemical Resource Engineering, Beijing University of Chemical Technology,Beijing,China,100029
- Author bio：
- Funds：
  
  Supported by the Program for New Century Excellent Talents in University(NCET-05-0122);the National Natural Science Foundation of China(20576008,20706003)
- DOI：
  中图分类号：
- 纸质出版：2010
- Accepted：
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张卫东, 崔春花, 杨彦强. Mass Transfer of Copper(Ⅱ) in Hollow Fiber Renewal Liquid Membrane with Different Carriers[J]. 中国化学工程学报（英文版）, 2010,18(2):346-350.

ZHANG Weidong, CUI Chunhua, YANG Yanqiang. Mass Transfer of Copper(Ⅱ) in Hollow Fiber Renewal Liquid Membrane with Different Carriers[J]. , 2010, 18(2): 346-350.
张卫东, 崔春花, 杨彦强. Mass Transfer of Copper(Ⅱ) in Hollow Fiber Renewal Liquid Membrane with Different Carriers[J]. 中国化学工程学报（英文版）, 2010,18(2):346-350. DOI：

ZHANG Weidong, CUI Chunhua, YANG Yanqiang. Mass Transfer of Copper(Ⅱ) in Hollow Fiber Renewal Liquid Membrane with Different Carriers[J]. , 2010, 18(2): 346-350. DOI：

摘要

Abstract

The extraction ability of organophosphorus extractant D2EHPA(di-2-ethylhexyl phosphoric acid) and hydroximic extractant Lix984N are investigated by the extraction equilibrium experiments.Effects of carrier concen-tration and organic/aqueous volume ratio on the mass transfer of hollow fiber renewal liquid membrane(HFRLM) are studied.Results show that

in the extracting process

kerosene and

-heptane are more suitable than methyl-isobutyl ketone

butylacetate and benzene as the diluents of D2EHPA or Lix984N.The favorable feed pH is 4.4 for D2EHPA and 2.6 for Lix984N.The mass transfer flux of HFRLM increases with carrier concentration and finally reaches a plateau.The mass transfer flux and the overall transfer coefficient increase with the organic/aqueous volume ratio

reach the maximum and then decrease.

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