A new bulk liquid membrane process for recovery of copper from dilute
ammoniacal leach solutions has been studied. Copper was extracted and
concentrated by means of a rotating film pertractor using LIX(R) 54 as
carrier. Assuming the existence of two thin reaction layers in the fe
ed and strip solutions, adjacent to both water-oil interfaces, a mathe
matical model was developed to describe the copper transport. On the b
asis of the experimental data obtained under various conditions and th
e model proposed it was found that the extraction step is controlled m
ainly by the mass transfer resistance, whereas the stripping mte of co
pper is controlled simultaneously by the rate of the mass transfer and
the rate of copper-complex decomposition in the stripping side reacti
on layer.