4.5 Article

Extraction Kinetics of Lanthanum in Chloride Medium by Bifunctional Ionic Liquid [A336][CA-12] Using a Constant Interfacial Cellwith Laminar Flow

Journal

CHINESE JOURNAL OF CHEMICAL ENGINEERING
Volume 22, Issue 10, Pages 1174-1177

Publisher

CHEMICAL INDUSTRY PRESS
DOI: 10.1016/j.cjche.2014.09.010

Keywords

Extraction kinetics; Bifunctional ionic liquid; Constant interfacial cell with laminar flow

Funding

  1. National Natural Science Foundation of China [51174184]
  2. National Basic Research Program of China [2012CBA01202]
  3. Key Research Program of the Chinese Academy of Sciences [KGZD-EW-201-1]
  4. Science and Technology Plan of Nantong City [BK2013030]
  5. University Science Research Project of Jiangsu Province [14KJB150019]
  6. Open Subject of Changchun Institute of Applied Chemistry, Chinese Academy of Sciences [RERU2014016]

Ask authors/readers for more resources

The extraction kinetics of La(III) from aqueous chloride solutions into n-heptane solutions of bifunctional ionic liquid extractant [A336][CA-12] (tricaprylmethylammonium sec-octylphenoxy acetic acid) was investigated using a constant interfacial cell with laminar flow. The effects of stirring speed, temperature and specific interfacial area on the extraction rate were examined. The results indicate that mass transfer kinetics of La(III) is a mixed-controlled process influenced by interfacial reaction. On the basis of mass transfer kinetic results in the extraction of La(III) by [A336][CA-12], the extraction rate equation of La(III) is proposed in terms of pseudo-first-order constants, which is supported by the measured thermodynamic equations. The mass-transfer kinetic model deduced from the rate controlling step is adequate to interpret the experimental data qualitatively. (C) 2014 The Chemical Industry and Engineering Society of China, and Chemical Industry Press. All rights reserved.

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