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In relation to this article, we declare that there is no conflict of interest.
Publication history
Received June 7, 2004
Accepted August 30, 2004
articles This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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One-through Selective Separation of Copper, Chromium and Zinc Ions by Hollow Fiber Supported Liquid Membrane

Department of Chemical Engineering, Chulalongkorn University, Payatai Road Bangkok, 10330, Thailand
ura.p@chula.ac.th
Korean Journal of Chemical Engineering, November 2004, 21(6), 1212-1217(6), 10.1007/BF02719496
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Abstract

The separation of a mixture of Cu(II), Cr(VI) and Zn(II) simultaneously from a sulfate media using two consecutive hollow fiber microporous liquid membrane extraction systems has been studied. The experiments were made in the one-through mode. LIX84-I and Aliquat336 were used as carrier extractants for copper and chromium in the first and second hollow fiber modules, respectively. Pure copper and pure chromium ions are extracted and stripped from first and second hollow fiber modules, respectively, but zinc ions cannot be extracted by both extractants due to pH conditions used in this study and remain in the raffinate. Results indicate that the percentage of extraction is highly dependent on pH of the feed solution and the pH value is 2.5 for the maximum extraction. The percentage of extraction of copper and chromium ions is enhanced when the concentration of LIX84-I and Aliquat336 is increased of which both maximum value is 0.5M, and these results also occur in stripping phase. The influence of sulfuric acid and sodium hydroxide concentration in strip solution of each column was examined, and it was found that the percentage of extraction and stripping is further increased due to the difference of driving force. The maximum percentage of extraction for copper is 33% and 92% for chromium. The experimental results indicated the feasibility of separation and recovery of these metals from the dilute solution by using membrane technology.

References

Alguacil FJ, Hydrometallurgy, 65, 9 (2002) 
Berta G, Ane MU, Ana IA, Ind. Eng. Chem. Res., 33 (1994)
Campderros ME, Acosta A, Marchese J, Talanta, 47, 19 (1998) 
Fernado V, Haris A, Sep. Sci. Technol., 35, 9 (2000)
Francisco JA, Antonio C, J. Chem. Technol. Biotechnol., 74 (1999)
Gherrou A, Kerdjoudj H, Desalination, 144(1-3), 231 (2002) 
Kyuchoukov G, Zhirkova S, Borowiak-Resterna A, Szymanowski J, Ind. Eng. Chem. Res., 39 (2000)
Loiacono O, Drioli E, Molinari R, J. Membr. Sci., 28 (1986)
Nakararueng K, "Extraction and Recovery of Copper, Chromium and Zinc Ions From Mixture Solution of Ion by Using Continuous Hollow Fiber Supported Liquid Membrane Technique," Master Thesis, Chulalongkorn University at Bangkok Thailand (2004)
Pattaweekongka W, Vijitchalermpong N, Pancharoen U, Korean J. Chem. Eng., 20, 6 (2003)
Porter C, Hadnbook of Industrial Membrane Technology, New Jersey, Noyes Publications (1990)
Ramakul P, Pancharoen U, Korean J. Chem. Eng., 20, 4 (2004)
Ramakul P, "Separation of Mixture of Lanthanum and Neodymium by Hollow Fiber Supported Liquid Membrane," Master Thesis, Chulalongkorn University at Bangkok Thailand (2002)
Sarangi K, Das RP, Hydrometallurgy, 71 (2004)
Schulz G, Desalination, 68, 191 (1988) 
Seiler GH, Asrid Sigel and Helmut Dekker, Inc. Handbook on Metals in Clinical and Analytical Chemistry (1994)
Sheng S, Mastuyama H, Teramoto M, Sep. Purif. Technol., 36, 17 (2004) 
Thornton D, "Science and Practice of Liquid-Liquid Extraction," 2, Clarendon Press (1992)

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