A liquid membrane (pertraction) process of copper recovery from dilute
aqueous solutions is studied applying a rotating film pertraction tec
hnique. LIX 65(R)N dissolved in C-10-C-13 normal paraffins is used as
the carrier. A mathematical model describing copper transfer is propos
ed, assuming that (1) the chemical reactions between copper ions and c
arrier molecules take place in the aqueous solution layers adjacent to
the membrane phase, and (2) both the reaction kinetics and the mass t
ransfer of the solutes control the overall rate of the process, In ord
er to evaluate the reaction rate constants and the coefficients of mas
s transfer, the distribution coefficients for the active oxime carrier
(m(HR)) and the copper-oxime complex (m(CuR2)) are obtained independe
ntly. The effects of temperature and disc rotation velocity on the per
traction rate are studied, as well as the possibility for the selectiv
e removal of copper from a solution containing ions of several bivalen
t metals. (C) 1997 Elsevier Science B.V.