The extraction kinetics of the Cu-LIX84 system was carried out in a Le
wis type cell. The Cu extraction rate increased with increasing temper
ature, pH and initial metal ion concentration. The extraction rate als
o increased with increasing revolution speed of the impeller up to 250
rpm and thereafter it had hardly any effect. The apparent activation
energy was found to be 40.6 KJ.mole(-1) which suggested that the rate
limiting step is the diffusion of Cu ion from the aqueous phase to the
interface for the formation of the Cu-LIX84 complex. The extraction r
ate favoured lower acid concentrtion as the activity of the Cu ion inc
reased with decreasing acid concentration. The equilibrium constant fo
r extraction process was found out.