Kinetics of Mn(II) extraction by D2EHPA
The kinetics of forward extraction of Mn(II) from 0.1 M SO 4 2− medium by di-(2-ethyl hexyl) phosphoric acid (D2EHPA) solution in kerosene have been investigated by the Lewis (L.C.) and Hahn cell (H.C.) techniques. For kinetic data treatment, both pseudo-rate constant, ‘ q’ or ‘rate/area’ and flux,...
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Published in | Hydrometallurgy Vol. 69; no. 1; pp. 145 - 156 |
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Main Authors | , |
Format | Journal Article |
Language | English |
Published |
Amsterdam
Elsevier B.V
01.04.2003
Elsevier |
Subjects | |
Online Access | Get full text |
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Summary: | The kinetics of forward extraction of Mn(II) from 0.1 M SO
4
2− medium by di-(2-ethyl hexyl) phosphoric acid (D2EHPA) solution in kerosene have been investigated by the Lewis (L.C.) and Hahn cell (H.C.) techniques. For kinetic data treatment, both pseudo-rate constant, ‘
q’ or ‘rate/area’ and flux, ‘
F’ methods have been applied. The empirical rate equations have been derived. Results have been compared among themselves and other published works on Mn(II)–D2EHPA systems. The rate constants obtained from the ‘
q’ and ‘
F’ methods differ in magnitude and units and an explanation of this has been given.
An analysis of the rate equations obtained from the Lewis cell technique suggests that the reaction: Mn
2++HA
2(i)
−→[Mn(HA
2)]
(i)
+occurring at the interface is the slowest. High activation energy,
E
a, in the lower temperature region (l.t.r.; 53 kJ mol
−1) supports the above mechanism. But the low
E
a value in the higher temperature region (h.t.r.; 10 kJ mol
−1) suggests a diffusion controlled reaction at the interface. In the Hahn cell experiments,
E
a never exceeds 12 kJ mol
−1 and so the process is entirely diffusion controlled in this cell at any temperature. The rate constant obtained from the Lewis and Hahn cell techniques using either ‘
F’ or ‘
q’ method differs widely (
k
L.C.=100
k
H.C.) and an explanation has been given. |
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ISSN: | 0304-386X 1879-1158 |
DOI: | 10.1016/S0304-386X(03)00004-5 |