Combined high-pressure acid leaching method for cobalt alloy and oxide cobalt minerals
A technology of cobalt oxide ore and cobalt alloy, which is applied in the field of cobalt hydrometallurgy, can solve the problems of low cobalt leaching rate, no mention of copper leaching efficiency, and needs to be verified, so as to achieve efficient leaching, reduce risks, and improve reliability Effect
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Embodiment 1
[0021] Grind the copper-cobalt alloy containing 13.24wt% cobalt, 14.01wt% copper, 64wt% iron, and 1.52wt% silicon until it passes through a 200 mesh sieve, and mix it with an initial concentration of 2mol / L at a liquid-solid ratio of 10:1 Sulfuric acid solution was mixed, the reaction temperature was set to 90°C, the stirring speed was 300r / min, and leaching was carried out at normal pressure for 6 hours; the leached residue and ball milled to a 200-mesh sieve containing 11.05wt% cobalt, 2.92wt% copper, and 3.09wt% iron %, sulfur 0.021wt% hydrocobalt ore, mixed at a mass ratio of 1:2, and then mixed with water at a liquid-solid ratio of 10, the initial acidity was controlled to be 1.5mol / L, the temperature in the kettle was 200°C, and the stirring speed was 300r / min After reacting for 8 hours and filtering, the leaching results are as follows: the cobalt leaching rate is 99.85%, the slag contains 0.03% cobalt, the copper leaching rate is 99.86%, and the slag contains 0.02% cop...
Embodiment 2
[0023] Grind the copper-cobalt alloy containing 13.24wt% cobalt, 14.01wt% copper, 64wt% iron, and 1.52wt% silicon until it passes through a 200 mesh sieve. Sulfuric acid solution was mixed, the reaction temperature was set to 70°C, the stirring speed was 500r / min, and leaching was carried out at normal pressure for 10 hours; the leaching residue and ball milled to a 200-mesh sieve containing 6.05wt% cobalt, 4.92wt% manganese, and 8.62wt% copper %, iron 5.6wt%, sulfur 0.009wt% cobalt ore, mixed at a mass ratio of 1:8, and then mixed with water at a liquid-solid ratio of 4, the initial acidity was controlled to be 4mol / L, and the temperature in the kettle was 150°C. Stirring speed was 500r / min, reacted for 3 hours and then filtered. The leaching results were: cobalt leaching rate 99.94%, slag containing cobalt 0.014%, manganese leaching rate 99.96%, slag containing manganese 0.012%, copper leaching rate 99.93%, slag containing Copper 0.013%.
Embodiment 3
[0025] Grind waste nickel-cobalt alloys containing 16.32wt% cobalt, 50.72wt% nickel, 13.45wt% chromium, and 12.31wt% to pass through a 200 mesh sieve, and mix it with an initial concentration of 3mol / L sulfuric acid solution was mixed, the reaction temperature was set at 80°C, the stirring speed was 400r / min, and the normal pressure was leached for 8 hours; the leached slag and ball milled to a 200-mesh sieve containing 11.05wt% cobalt, 2.92wt% copper, and 3.09% iron. Wt%, sulfur 0.021wt% hydrocobalt ore, mixed at a mass ratio of 1:4, and then mixed with water at a liquid-solid ratio of 6, the initial acidity was controlled at 2mol / L, the temperature in the kettle was 180°C, and the stirring speed was 400r After reacting for 6 hours, the leaching results were: cobalt leaching rate 99.8%, slag containing cobalt 0.05%, nickel leaching rate 99.7%, slag containing nickel 0.065%, copper leaching rate 99.88%, slag containing copper 0.04%.
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