Method for recovering cobalt from inverse antimony purified cobalt residue
A technology for cobalt slag and cobalt precipitation, which is applied in the field of hydrometallurgy, can solve the problems of impurities brought by oxidants, reduce the grade of cobalt concentrate, and incomplete removal of iron and manganese, and achieve the effect of improving the grade.
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Embodiment 1
[0032] (1) Leaching: reverse antimony purified cobalt slag (containing 0.2wt% cobalt, 20wt% zinc, 15wt% lead, 7wt% cadmium, 5wt% copper, 1wt% iron, 300g / t silver, 600g / t germanium) dry weight 1t , together with 2t of produced water, put into the mechanical stirring tank, stir, heat up to 88°C, add 40wt% sulfuric acid solution evenly and slowly to the mixed material liquid, stop adding sulfuric acid solution when the pH value of the mixed material liquid drops to 2.5, when When the pH value rises to 4.0, add sulfuric acid solution slowly and evenly again, and circulate like this until the pH value no longer rises, add a small amount of cobalt slag to raise the pH value to 4.0, filter the mixed material liquid to obtain leaching liquid and leaching residue respectively; the obtained leaching residue Containing 31.25wt% lead, 9.6wt% copper, 0.11wt% germanium, and 625g / t silver, the leach slag is sent to crude lead smelting to recover lead, silver, and copper, and then sent to fumi...
Embodiment 2
[0036] (1) Leaching: Antimony-purified cobalt slag (containing 1wt% cobalt, 15wt% zinc, 10wt% lead, 5wt% cadmium, and 1.5wt% iron) with a dry weight of 1t is added to the mechanical stirring tank together with 2.5t of production water , stir, heat up to 90°C, add 35% sulfuric acid solution evenly and slowly to the mixture liquid, stop adding sulfuric acid solution when the pH value of the mixture liquid drops to 2.5, and slowly and uniformly add sulfuric acid solution again when the pH value rises to 4.0 , circulate like this until the pH value no longer rises, add a small amount of cobalt slag to raise the pH value to 4.0, filter the mixed material liquid to obtain the leaching liquid and leaching residue respectively; the obtained leaching residue contains 22.2wt% of lead and 6.7wt% of zinc. The slag is sent to crude lead smelting to recover lead, and then to fuming furnace to recover zinc; the resulting leachate contains 4.45g / l cobalt, 55g / l zinc, 22g / l cadmium, and 2.0g / l ...
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