The recovery of Cu(II) from ammoniacal
solutions with the sandwich
supported liquid membrane was studied by using 4-ethyl-1-phenyl-1,3-octadione
as the carrier. The transport behavior of Cu(II), membrane stability
and selectivity were investigated. The transport efficiency of Cu(II)
in the membrane module is evidently dependent on the feed pH, carrier
concentration, phase ratio and temperature, but almost independent
of the H2SO4 concentration in receiving phase.
The increase of carrier concentration and temperature can simultaneously
enhance Cu(II) transport and initial copper flux in the feed phase,
while both of them decrease as the phase ratio increases. The initial
copper flux can reach 759 mmol m–2 h–1 at 45 °C. A satisfied membrane stability was obtained, and
the copper concentration in the receiving phase can reach 3.91 g L–1 via uphill transport after five cycles. The main
transport resistance could derive from the diffusion process of the
copper complexes through the receiving phase/membrane interface. Moreover,
the Cu(II) can be selectively recovered over Ni(II) and Zn(II). The
high flux and good membrane stability makes the system promising for
recovering metal values from various industrial process effluents.