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Received June 3, 2005
Accepted September 20, 2005
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Permeation study on the hollow-fiber supported liquid membrane for the extraction of Cobalt(II)
Department of Chemical Engineering, Faculty of Engineering, Chulalongkorn University, Bangkok, Thailand 1Department of Chemical Engineering, Faculty of Engineering and Industrial, Technology of Silpakorn University, Sanam Chandra Campus, Nakhonphthom, Thailand 2Department of Organic Technology, Faculty of Chemical Technology, Slovak University of Technology, Bratislava, Slovakia (Slovak Republic)
ura.p@chula.ac.th
Korean Journal of Chemical Engineering, January 2006, 23(1), 117-123(7), 10.1007/BF02705702
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Abstract
.The transport of Co(II) through hollow-fiber-supported liquid membrane containing di-(2-ethylhexyl) phosphoric acid (D2EHPA) diluted in kerosene was examined. The mass transfer rate, expressed as permeability, P, focused on diffusion through the aqueous layer in the feed solution, the organic layer and the aqueous layer in the stripping solution. Experiments were performed as a function of aqueous feed solution velocity (100-500 ml/min), carrier concentration (0.1-20% v/v), aqueous stripping solution velocity (100-1,000 ml/min) and feed concentration (100-1,000ppm) with 0.1M HCl in the product phase. pH of the feed solution was 5.0. The measured permeabilities were compared to generally accepted mass transfer correlations. The validity of the prediction was evaluated with the experimental data, and the data were found to tie in well with the theoretical values. The model is the reported describing that the rate limiting step in the transport of the ion was the diffusion through both aqueous films, feed and stripping, whereas the organic resistance of the membrane was negligible. From this study, the model has good potential for the prediction of permeability of Co(II).
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References
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Breembroek GRM, Witkamp GJ, van Rosmalen GM, J. Membr. Sci., 147(2), 195 (1998)
Campderros ME, Marchese J, J. Membr. Sci., 164(1-2), 205 (2000)
Drioli E, Loiacono O, Molinari R, Pantano G, Chimicaoggi, 4, 25 (1989)
Gabelman A, Hwang S, J. Membr. Sci., 61, 159 (1999)
Gherrou A, Kerdjoudj H, Desalination, 144(1-3), 231 (2002)
Haan AB, Bartels PV, Grauw J, J. Membr. Sci., 45, 281 (1989)
Jakubec K, Haman J, Rod V, Hydrometallurgy, 17, 12 (1986)
Kumar A, Haddad R, Benzal G, Ninou R, Sastre AM, J. Membr. Sci., 174(1), 17 (2000)
Leveque X, Ann. Mines., 13, 201 (1928)
Loiacono O, Drioli E, Molinari R, J. Membr. Sci., 28, 123 (1986)
Marchese J, Campderrds ME, Acosta A, J. Chem. Technol. Biotechnol., 57, 37 (1993)
Porter C, Handbook of industrial membrane technology, New Jersey, Noyes Publications (1990)
Prakorn R, Ura P, Korean J. Chem. Eng., 20(4), 724 (2003)
Prakorn R, Kwanta N, Ura P, Korean J. Chem. Eng., 21(6), 1212 (2004)
Rathore NS, Sonawane JV, Kumar A, Venugopalan AK, Singh RK, Bajpai DD, Shukla JP, J. Membr. Sci., 189, 119 (2002)
Seider EN, Tate GE, Ind. Eng. Chem., 28, 1429 (1936)
Sheng S, Mastuyama H, Teramoto M, Sep. Purif. Technol., 36, 17 (2004)