In this paper, we examine the possibility of using membrane extraction
and supported liquid membranes to recover gallium from alkaline solut
ions. Membrane extraction proves to be an alternative process to recov
er gallium from such liquors. In order to maximize mass transfer, high
ly hydrophilic membranes should be used in both the membrane extractio
n and stripping processes. The optimum composition of the membrane ext
ractant is 10-15% Kelex 100, 10% n-decanol, 5% Versatic 10, and kerose
ne (vol %). The highest gallium permeability was obtained when the fee
d solution contained about 1.5 mol/L sodium hydroxide. The supported l
iquid membrane used failed to transport gallium because of instability
. The dominant mechanisms for failure are considered to be spontaneous
formation of a water-in-oil emulsion and formation of precipitates, c
ausing membrane pore obstruction.