The extraction equilibria of Co(II) from 1.0 M KCl medium by the comme
rcial extractant Cyanex 301 dissolved in toluene has been studied. The
effects of pH, extractant concentration and metal concentration on th
e extraction behaviour have been examined. Experimental data have been
treated graphically and numerically and can be explained by assuming
the extraction of the dominant species CoL2. HL being bis(2,4,4-trimet
hylpentyl)dithiophosphinic acid, the major component of Cyanex 301. Th
e numerical treatment also indicated the extraction of a minor species
of probable stoichiometry CoClL(HL)), but whereas the former species
has been clearly identified, the latter species, probably due to the f
act that its contribution to the extraction process is very little, ca
n only be considered as an approximation as its stoichiometry is not d
efined precisely by this numerical treatment. Conditional equilibrium
constants of the extraction process are also given.