A non-saponification method for extraction separation of nickel and cobalt
A non-saponification, nickel-cobalt technology, applied in the field of solid waste separation, can solve the problem of solution acidity enhancement, achieve low equipment requirements, avoid excessive discharge, and achieve the effect of great industrial practicability
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Embodiment 1
[0026] The positive electrode material powder of the waste power lithium-ion battery is roasted in a high-temperature atmosphere of 600 ° C for 2 hours, and the black positive electrode active material is decomposed, so as to facilitate the subsequent acid leaching.
[0027] The roasted black matter is pickled in hydrochloric acid. The pickling conditions are: acid concentration 2mol / L, solid-liquid ratio 6g / 100ml, temperature 90°C, time 50min. Adjust the pH of the pickling solution to 3 with sodium hydroxide.
[0028] Use P204 to remove impurity elements in the pickling solution by extraction, and take the water phase (the pH value of this water phase is 3).
[0029] Take the acid leaching solution (water phase) after impurity removal and the co-extraction extractant to carry out the extraction reaction, wherein the volume ratio of B236:N204 in the co-extraction agent is 1:6, and the volume ratio of the sum of the two extractants to kerosene is 1:4, the pH value of the acid ...
Embodiment 2
[0032] The positive electrode material powder of the waste power lithium-ion battery is roasted in a high-temperature atmosphere of 650°C for 2 hours, and the black positive electrode active material is decomposed, so as to facilitate the subsequent acid leaching.
[0033] The roasted black matter is pickled in hydrochloric acid. The pickling conditions are: acid concentration 2mol / L, solid-liquid ratio 6g / 100ml, temperature 90°C, time 50min. Use sodium hydroxide to adjust the pH value of the pickling solution to 3.5, and use P204 to remove impurity elements in the pickling solution.
[0034] Take the impurity-removed acid leaching solution and the co-extraction agent for extraction reaction, wherein the volume ratio of B236:N204 in the co-extraction agent is 1:7, and the volume ratio of the co-extraction agent to kerosene is 1:4, and the acid leaching is controlled during extraction. The pH of the liquid is 3.5, and the volume ratio of the synergistic extractant / water phase i...
Embodiment 3
[0036] The difference between the operating conditions of this example and the example is that sodium hydroxide is used to adjust the pH value of the pickling solution to 4.0, and then P204 is used to remove impurity elements in the pickling solution.
[0037] Other operations are the same as in Example 2. The lower aqueous phase was separated after the extraction was allowed to stand for stratification. It was measured that the extraction rate of cobalt reached 84.5%, and the extraction rate of nickel reached 7%.
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