The transfer and separation of Cu(II), Co(II), Ni(II) and Zn(II) ions
across a hollow fiber supported liquid membrane containing LIX 864 as
the mobile carrier dissolved in kerosene solvent has been investigated
. The flux and selectivity for copper has been studied as a function o
f the feed flow, the carrier concentration in the liquid membrane and
the extraction solution acidity. A maximum copper recovery at 30% of L
IX (v/v) in the diluent was obtained. The permeation experiments showe
d that at pH 2 in the extraction solution a highly selective separatio
n of Cu over the other cations can be achieved. Increasing the acidity
of the extraction solution copper selectivity decrease and the grade
of recuperation sequence is Cu > Co > Ni > Zn. These results suggest t
hat in selected situations, this membrane system can be competitive wi
th the conventional liquid-liquid extraction process, in particular in
leaching solutions with low metal concentration. (C) 1998 Elsevier Sc
ience B.V. All rights reserved.