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Device for separating lithium and ternary metal ions M from lithium solution

A ternary metal and lithium solution technology, which is applied in the recycling of waste collectors, etc., can solve the problems of low lithium recovery rate, high recovery cost, and high processing cost, so as to reduce production costs and operating requirements, and avoid the use of extractants , the effect of avoiding alkali metal pollution

Active Publication Date: 2022-07-22
广东芳源新材料集团股份有限公司 +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The advantage of wet treatment is that the recovery rate is high, which can reach about 90%, but the treatment process is complicated and the treatment cost is relatively high
And in the wet recovery process, lithium can usually be extracted last. Generally, after extracting metal ions such as cobalt, manganese, and nickel, most of the remaining lithium elements are in the raffinate, because the lithium content in the raffinate is low at this time. (Generally 1.5~2.0g / L), making it more difficult to enrich again, the recovery cost is high by means of evaporation, concentration and crystallization, and it is often not recovered, and the tail water is discharged after treatment, causing environmental pollution and waste of resources
The fire method refers to adding the positive electrode powder to the slagging agent and then melting the slag at a high temperature above 1300°C to separate valuable metals. Although the fire method has a large amount of treatment and a simple process, the recovery rate of lithium is very low. The current industry basically no use
[0003] Therefore, in addition to the extraction method, how to separate lithium and ternary metal ions M (nickel, cobalt, manganese, aluminum, etc.) The efficient separation of ions M, further and how to realize lithium recovery from the source of battery waste and low content (generally 1.5~2.0g / L) lithium recovery related technologies and recovery devices have not yet been reported.

Method used

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  • Device for separating lithium and ternary metal ions M from lithium solution
  • Device for separating lithium and ternary metal ions M from lithium solution
  • Device for separating lithium and ternary metal ions M from lithium solution

Examples

Experimental program
Comparison scheme
Effect test

Embodiment approach 1

[0093] Lithium sulfate solution containing ternary metal ion M (nickel), nickel concentration of 120g / L, lithium concentration of 18.0g / L, lithium sulfate solution containing ternary metal ion M (nickel) together with sodium hydroxide solution and ammonia water Enter the synthesis reaction kettle, control the stirring speed to be 160 rpm, the pH value to be 12.0, and the synthesis temperature to be 60 ° C. After the reaction kettle is full, it overflows normally, and the overflowed slurry is separated from solid and liquid by a centrifuge, and the ternary metal ion M is realized. (Ni) effective separation of M and lithium in lithium sulfate solution, and detection of residual lithium in the obtained spherical nickel hydroxide and residual M content in lithium sulfate solution.

Embodiment approach 2

[0095] Lithium sulfate solution containing ternary metal ion M (nickel), nickel concentration of 120g / L, lithium concentration of 25.0g / L, lithium sulfate solution containing ternary metal ion M (nickel) together with sodium hydroxide solution and ammonia water Enter the synthesis reaction kettle, control the stirring speed to be 160 rpm, the pH value to be 12.0, and the synthesis temperature to be 60 ° C. After the reaction kettle is full, it overflows normally, and the overflowed slurry is separated from solid and liquid by a centrifuge, and the ternary metal ion M is realized. (Ni) effective separation of M and lithium in lithium sulfate solution, and detection of residual lithium in the obtained spherical nickel hydroxide and residual M content in lithium sulfate solution.

Embodiment approach 3

[0097] Lithium sulfate solution containing ternary metal ion M (cobalt), cobalt concentration of 110g / L, lithium concentration of 30.0g / L, lithium sulfate solution containing ternary metal ion M (cobalt), potassium hydroxide solution, ammonia water together Enter the synthesis reaction kettle, control the stirring speed to be 160 rpm, the pH value to be 12.0, and the synthesis temperature to be 60 ° C. After the reaction kettle is full, it overflows normally, and the overflowed slurry is separated from solid and liquid by a centrifuge, and the ternary metal ion M is realized. The effective separation of M and lithium in the lithium sulfate solution of (cobalt), and the detection of the residual lithium in the obtained spherical cobalt hydroxide and the residual M content in the lithium sulfate solution.

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PUM

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Abstract

The invention provides a device for separating lithium and ternary metal ions M from a lithium solution. The device comprises a device body, and the device body is provided with a plurality of feed ports, an overflow port located in the side wall of the upper end of the device body and a discharge port located in the bottom of the device body; the stirring device is connected with the device body in a sealing manner and is used for stirring in the device body; the temperature control device wraps the outer side of the device body and is used for heating or cooling the device body; the device for separating the lithium and the ternary metal ions M from the lithium solution is used for enabling the ternary metal ions M in the lithium solution to form spherical hydroxide precipitates, and enabling the lithium in the lithium solution to be separated from the ternary metal ions M to obtain mother liquor. Compared with the prior art, the device is simple in structure, and production cost and operation requirements are reduced.

Description

technical field [0001] The invention belongs to the field of new energy materials, and in particular relates to a device for separating lithium and ternary metal ions M from a lithium solution. Background technique [0002] Lithium-ion batteries have developed rapidly in the battery market due to their special energy storage properties. However, as lithium batteries are used in charge and discharge cycles, they need to be recycled after their lifespan expires. At present, the general steps of recycling waste lithium-ion batteries are disassembly, screening, crushing and extraction, and the crushed cathode powder is then subjected to wet or fire processing to obtain the desired product. The advantage of wet treatment is that the recovery rate is high, up to about 90%, but the treatment process is complicated and the treatment cost is relatively large. In the wet recovery process, lithium is usually extracted last. Generally, after the extraction of cobalt, manganese, nickel ...

Claims

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Application Information

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IPC IPC(8): C22B26/12C22B23/00C22B47/00C22B21/00C22B7/00H01M10/54
CPCC22B26/12C22B23/0461C22B47/00C22B21/0023C22B7/006H01M10/54
Inventor 刘京星许健勇黄新强吴芳罗爱平
Owner 广东芳源新材料集团股份有限公司
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