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Nickel, cobalt and copper were separated by solvent extraction with P204. The experimental results show that [Co(NH 3) 6] 3+ is an inert complex in extraction kinetics, therefore cobalt can be separated from nickel and copper by non equilibrium solvent extraction. Under the conditions of temperature 25?℃, contact time of two phases 10?min, phase ratio 1∶1, aqueous pH 10.10 and concentration of P204 20%, [Co(NH 3) 6] 3+ is hardly extracted by P204, while the percentage extractions of nickel and copper are 79.3% and 93.9% respectively. Nickel and copper are separated by equilibrium solvent extraction with P204. Under the conditions of temperature 25?℃, contact time of two phases 1?min, phase ratio 1∶1, equilibrium pH 4.01 and concentration of P204 20%, the separation factor of copper and nickel is 216.
Nickel, cobalt and copper were separated by solvent extraction with P204. The experimental results show [Co (NH 3) 6] 3+ is an inert complex in extraction kinetics, therefore cobalt can be separated from nickel and copper by non equilibrium solvent extraction Under the conditions of temperature 25 ° C, contact time of two phases 10 min, phase ratio 1: 1, aqueous pH 10.10 and concentration of P204 20%, [Co (NH 3) 6] 3+ is preferably extracted by P204 , while the percentage extractions of nickel and copper are 79.3% and 93.9% respectively. Nickel and copper are separated by equilibrium solvent extraction with P204. Under the conditions of temperature 25? C, contact time of two phases 1? min, phase ratio 1 : 1, equilibrium pH 4.01 and concentration of P204 20%, the separation factor of copper and nickel is 216.