Method for extraction of Co and Ni with mixed leaching of Co slag and Ni-Mo ores
A technology of nickel-molybdenum ore and cobalt slag, which is applied in the field of metallurgy, can solve the problems of waste of precious tungsten resources, etc., and achieve the effects of less reagent consumption, simple treatment process, and high metal recovery rate
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Embodiment 1
[0051] (1) Ball milling of nickel-molybdenum ore: the nickel-molybdenum ore from Zunyi, Guizhou has been ball-milled in advance, and sieved through a 200-mesh screen. Its main components are:
[0052]
[0053] (2) Nickel-molybdenum ore and cobalt slag are mixed in a mass ratio (0.3:1): the chemical composition of cobalt slag is:
[0054]
[0055] (3) Leaching reaction process: the leaching reaction temperature is controlled at 85-90°C, the remaining acid concentration is about 20-30g / l, and the leaching reaction time is controlled for 3 hours.
[0056] According to the slag weight after leaching and the cobalt and nickel contents, the cobalt leaching rate is calculated to be 98.8% by weight, and the nickel leaching rate is 90.89% by weight. The content of molybdenum in the leaching slag is 5.17% by weight. The leached cobalt and nickel solutions can be further removed and purified to produce cobalt chloride and nickel sulfate. The leached molybdenum-containing slag can...
Embodiment 2
[0058] (1) nickel-molybdenum ore ball mill: with embodiment 1;
[0059] (2) Nickel-molybdenum ore and cobalt slag are mixed according to the mass ratio (0.25:1): the chemical composition of cobalt slag is:
[0060]
[0061] (3) Leaching reaction process: the leaching reaction temperature is controlled at 85-90°C, the residual acid concentration is about 22-30g / l, and the leaching reaction time is controlled for 3 hours.
[0062] According to the slag weight after leaching and the cobalt and nickel contents, the cobalt leaching rate is calculated to be 98.1% by weight, and the nickel leaching rate is 95.6% by weight. The content of molybdenum in the leaching slag is 4.97% by weight. The leached cobalt and nickel solutions can be further removed and purified to produce cobalt chloride and nickel sulfate. The leached molybdenum-containing slag can be used as raw material for molybdenum smelting system.
Embodiment 3
[0064] (1) nickel-molybdenum ore ball mill: with embodiment 1;
[0065] (2) Nickel-molybdenum ore and cobalt slag are mixed in a mass ratio (0.2:1): the chemical composition of cobalt slag is:
[0066]
[0067] (3) Leaching reaction process: the leaching reaction temperature is controlled at 85-90°C, the remaining acid concentration is about 26-30g / l, and the leaching reaction time is controlled for 3 hours.
[0068] According to the slag weight after leaching and the cobalt and nickel contents, the cobalt leaching rate is calculated to be 96.8% by weight, and the nickel leaching rate is 94.6% by weight. The content of molybdenum in the leaching slag is 3.93% by weight. The leached cobalt and nickel solutions can be further removed and purified to produce cobalt chloride and nickel sulfate. The leached molybdenum-containing slag can be used as raw material for molybdenum smelting system.
[0069] Evaluation and analysis: Embodiment 1-3 has studied respectively the influe...
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