Method of extracting nickel and cobalt from phosphoric acid leaching solution of laterite-nickel ores
A technology of laterite nickel ore and leaching solution, which is applied in the field of hydrometallurgy, can solve the problems of difficulty in organic reverse extraction of P507, difficulty in separation of high nickel and low cobalt solutions, and high impurity content, and achieves easy industrial application, fewer extraction stages, and simple process. Effect
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Embodiment 1
[0062] Step (1): Treat lateritic nickel ore by pre-roasting transformation-phosphoric acid atmospheric pressure leaching, pre-roasting temperature 400°C, roasting time 1h, phosphoric acid concentration 3mol / L, leaching temperature 90°C, leaching time 2h, leaching liquid-solid ratio 10: 1. After the leaching is completed, a section of leaching solution is obtained. The leaching rate of nickel is 98.43%, the leaching rate of cobalt is 89.69%, and the leaching rate of iron is 7.08%. The pH of the obtained leachate was 0.7, and the contents of main metal ions in the leachate were shown in Table 2.
[0063] Table 2 Concentration of metal element ions in leachate
[0064]
[0065] Step (2): Using ammonia water as an alkaline agent, adjust the pH of the leach solution obtained in step (1) to 3.0 to obtain the first impurity removal solution. At this time, the removal rates of aluminum, iron and manganese in the leach solution are 57.7% respectively , 91.2%, and 60.0%, and the los...
Embodiment 2
[0071] Compared with Example 1, the only difference is that in step (4), the extraction stages of P507 are three stages, and the cobalt extraction rates after three stages of extraction are 96.6% and 8.7%, respectively.
Embodiment 3
[0073] Compared with Example 1, the only difference is that in step (4), the extraction rates of cobalt and nickel after primary extraction are 54.2% and 2.5%, respectively. After the primary extraction through P507, the extraction rate of cobalt is low.
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