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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

Active Publication Date: 2018-03-02
BEIJING UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Patent CN1824814 proposes a mixed extractant that uses one or 2-3 kinds of acidic organic acids or organic acid ester extractants to extract and separate rare earth elements in rare earth chloride or rare earth nitrate solutions. When extracting and separating rare earths, the organic extractant does not need saponification, and no waste water is generated during the extraction process, which can eliminate the pollution of ammonia nitrogen wastewater to water resources. Although this method uses a composite extractant instead of saponification, the extractant is weakly acidic Organic phosphoric acid, this method improves the ability to extract and separate rare earths through the synergistic effect of the compound extractant, but it will lead to an increase in the acidity of the solution

Method used

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Examples

Experimental program
Comparison scheme
Effect test

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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Abstract

A non-saponification method for extraction separation of nickel and cobalt is provided. The method includes subjecting nickel- and cobalt-containing solid waste to high-temperature calcination, performing acid leaching to form an acid leachate, mixing synergistic extractants and a diluting agent, reacting the mixture with the acid leachate, and extracting the cobalt in the acid leachate to achievenickel-cobalt separation. No NaOH adopted as a saponifier is used in the method, thus avoiding excessive emission of saponification waste water. An acidic extractant B326 and an alkaline extractant methyl chloride N204 are synergistic under acidic conditions and the cobalt in the acid leachate is extracted into an organic phase effectively, thus achieving nickel-cobalt separation. For power battery solid waste the discharging amount of which is huge because power batteries are widely applied, the method is simple to operate and low in equipment requirements and has huge industrial practicality.

Description

technical field [0001] The invention belongs to the technical field of solid waste treatment, and in particular relates to a method for separating solid waste containing nickel and cobalt. Background technique [0002] With the rapid development of the automobile industry, problems such as environmental pollution, energy depletion, and resource shortage caused by traditional automobiles have become increasingly severe, and the proportion of new energy vehicles in my country's automobile industry has gradually increased. As a major part of the new energy vehicle industry chain, the performance of power batteries has also been improved. At present, the research on power batteries of new energy vehicles in my country mainly focuses on the improvement of safety performance and service life, but there is a serious disconnect in the recycling of power batteries. For example, lithium-ion batteries as power batteries do not contain heavy metal elements such as mercury, cadmium, and...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B7/00C22B1/02C22B23/00
CPCC22B1/02C22B7/007C22B23/0423C22B23/0453C22B23/0484
Inventor 席晓丽张政政马立文聂祚仁
Owner BEIJING UNIV OF TECH
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