Method for removing hexavalent chromium in process of preparing cobalt nickel hydroxide from laterite-nickel ore
A technology of nickel cobalt hydroxide and laterite nickel ore, which is applied in the field of metallurgy and can solve problems such as unqualified products
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Embodiment 1
[0054] Taking a laterite nickel mine in Indonesia as the implementation object, the chromium content in the laterite nickel mine is 1.37%. The laterite nickel ore is made into a slurry with a concentration of 28wt%, and the first reducing agent is added to the laterite nickel ore slurry, specifically a composite agent with a ratio of sulfur to pyrite of 1:1, which is mixed with the total amount of the laterite nickel ore. The mass ratio of chromium is 1:1. Preheat to 200°C, then heat up, and carry out high-pressure acid leaching under the conditions of reaction temperature 250°C, acid ore ratio 200Kg / t, and reaction time 1h. After high-pressure leaching, the concentration of hexavalent chromium is less than 0.5mg / L. The leaching rates were 95.25% and 91.04%, respectively.
Embodiment 2
[0056] The difference from Example 1 is only that the chromium content in the laterite nickel ore is 2.14%, the first reducing agent is sulfur alone, the mass ratio of the first reducing agent to the total chromium in the laterite nickel ore is 1:3, and the content of Ni and Co The leaching rates are 95.81% and 91.45% respectively; the concentration of hexavalent chromium after high pressure leaching is less than 0.5mg / L.
Embodiment 3
[0058] The difference from Example 1 is only that the chromium content in the laterite nickel ore is 2.42%, the ratio of sulfur to pyrite is 4:1, the reaction temperature is 250°C, and the leaching rates of Ni and Co are 97.14% and 96.45% respectively; After high pressure leaching, the concentration of hexavalent chromium is <0.5mg / L.
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