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Hancil, V., Slater, M.J., Yu, W. (1990) On the possible use of di-(2-ethylhexyl) phosphoric acid/zinc as a recommended system for liquid-liquid extraction: the effect of impurities on kinetics. Hydrometallurgy, 25 (3). 375-386 doi:10.1016/0304-386x(90)90052-4

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Reference TypeJournal (article/letter/editorial)
TitleOn the possible use of di-(2-ethylhexyl) phosphoric acid/zinc as a recommended system for liquid-liquid extraction: the effect of impurities on kinetics
JournalHydrometallurgy
AuthorsHancil, V.Author
Slater, M.J.Author
Yu, W.Author
Year1990 (January)Volume25
Issue3
PublisherElsevier BV
DOIdoi:10.1016/0304-386x(90)90052-4Search in ResearchGate
Generate Citation Formats
Mindat Ref. ID7887078Long-form Identifiermindat:1:5:7887078:5
GUID0
Full ReferenceHancil, V., Slater, M.J., Yu, W. (1990) On the possible use of di-(2-ethylhexyl) phosphoric acid/zinc as a recommended system for liquid-liquid extraction: the effect of impurities on kinetics. Hydrometallurgy, 25 (3). 375-386 doi:10.1016/0304-386x(90)90052-4
Plain TextHancil, V., Slater, M.J., Yu, W. (1990) On the possible use of di-(2-ethylhexyl) phosphoric acid/zinc as a recommended system for liquid-liquid extraction: the effect of impurities on kinetics. Hydrometallurgy, 25 (3). 375-386 doi:10.1016/0304-386x(90)90052-4
In(1990, January) Hydrometallurgy Vol. 25 (3) Elsevier BV

See Also

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Svendsen, H.F., Schei, G., Osman, M. (1990) Kinetics of extraction of zinc by di (2-ethylhexyl) phosphoric acid in cumene. Hydrometallurgy, 25 (2). 197-212 doi:10.1016/0304-386x(90)90039-5
Veglio', F., Slater, M.J. (1996) Design of liquid-liquid extraction columns for the possible test system Zn/D2EHPA in n-dodecane. Hydrometallurgy, 42 (2). 177-195 doi:10.1016/0304-386x(95)00083-s
Sato, Taichi, Kikuchi, Shoji (1988) Liquid-liquid extraction of tin(IV) from hydrochloric acid solutions by di( 2-ethylhexyl) phosphoric acid. Hydrometallurgy, 20 (1). 97-108 doi:10.1016/0304-386x(88)90029-1
Lukas, W., Kapala, Z. (1979) Empirical model for the extraction system YCl3ErCl3HClH2ODI-(2-ethylhexyl)phosphoric acid—n-heptane. Hydrometallurgy, 4 (3). 279-284 doi:10.1016/0304-386x(79)90018-5
MacLean, D.W.J., Dreisinger, D.B. (1993) The kinetics of zinc extraction in the di(2-ethylhexyl) phosphoric acid, n-heptane-Zn(ClO4)2, HClO4, H2O system using the rotating diffusion cell. Hydrometallurgy, 33 (1). 107-136 doi:10.1016/0304-386x(93)90009-3
Slater, M.J. (1989) Liquid-liquid extraction. Hydrometallurgy, 22 (1). 281pp. doi:10.1016/0304-386x(89)90059-5
Bukowsky, H., Uhlemann, E., Gloe, K., Mühl, P. (1992) The separation of calcium and magnesium from lithium chloride by liquid-liquid extraction with di (2-ethylhexyl) phosphoric acid. Hydrometallurgy, 28 (3). 323-329 doi:10.1016/0304-386x(92)90037-z
Matsuyama, Hideto, Miyake, Yoshikazu, Izumo, Yoshitsugu, Teramoto, Masaaki (1990) Kinetics and mechanism of metal extraction with acidic organophosphorus extractants (II): Extraction mechanism of Fe(III) with Di(2-ethylhexyl) phosphoric acid. Hydrometallurgy, 24 (1). 37-51 doi:10.1016/0304-386x(90)90074-c
Forrest, C., Hughes, M.A. (1978) The separation of zinc from copper by di-2-ethylhexyl phosphoric acid - an equilibrium study. Hydrometallurgy, 3 (4). 327-342 doi:10.1016/0304-386x(78)90037-3
Amer, S., Figueiredo, J.M., Luis, A. (1995) The recovery of zinc from the leach liquors of the CENIM-LNETI process by solvent extraction with di(-2-ethylhexyl)phosphoric acid. Hydrometallurgy, 37 (3). 323-337 doi:10.1016/0304-386x(94)00040-a
Holdich, R.G., Lawson, G.J. (1985) The solvent extraction of lead from chloride solutions using di(2-ethylhexyl)phosphoric acid. Hydrometallurgy, 14 (3). 387-393 doi:10.1016/0304-386x(85)90046-5
 
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