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Method for recovering and extracting lithium

A technology for extracting lithium and organic extractant, applied in the field of lithium recovery and extraction, can solve the problems of co-extraction effect, increased sludge treatment cost, increased post-treatment load, etc., so as to simplify the extraction operation process and avoid hydroxides. The effect of precipitation and reduction of post-processing load

Active Publication Date: 2019-11-19
哈工(芜湖)新材料科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In the process of adjusting the pH, a large amount of alkaline substances such as sodium hydroxide solid or solution are often added, resulting in the enlargement of the solution volume and the generation of a large amount of sediment, resulting in an increase in post-treatment load and an increase in sludge treatment costs.
In addition, waste treatment, recycling battery treatment or other raw material treatment with multi-element components can easily cause serious co-extraction effects and lose a large amount of other elements, especially when the elements in the raw material to be extracted are complex, it may be possible to simply extract a single element. Cause multiple elements to interfere at the same time and cannot be effectively purified

Method used

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  • Method for recovering and extracting lithium
  • Method for recovering and extracting lithium
  • Method for recovering and extracting lithium

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0046] a. Add 0.2g of solid sodium hydroxide to 10ml of Cyanex272, stir with a magnet, add 5ml of absolute ethanol and heat to above 50°C for about three hours, wait for the complete evaporation of absolute ethanol (can be determined by comparing with the original oil phase liquid level) Judging volatilization), saponified Cyanex272 was obtained;

[0047] b. Add 2g of solid sodium hydroxide to 50ml of kerosene, stir with a magnet, add 25ml of absolute ethanol and heat to above 50 degrees for about three hours, wait for the complete evaporation of absolute ethanol (can be judged by comparing with the original oil phase liquid level) Volatility), since the present embodiment prepares saturated saponified kerosene, the added solid sodium hydroxide is excessive, so the saponified product is filtered through 100 mesh filter paper to remove excess solid sodium hydroxide, and saturated saponified kerosene is obtained;

[0048] c. Take 1.2ml of saponified Cyanex272 and 8.8ml of satura...

Embodiment 2

[0054] a. Add 0.2g of solid sodium hydroxide to 10ml of Cyanex272, stir with a magnet, add 5ml of absolute ethanol and heat to above 50°C for about three hours, wait for the complete evaporation of absolute ethanol (can be determined by comparing with the original oil phase liquid level) Judging volatilization), saponified Cyanex272 was obtained;

[0055] b. Add 2g of solid sodium hydroxide to 50ml of kerosene, stir with a magnet, add 25ml of absolute ethanol and heat to above 50 degrees for about three hours, wait for the complete evaporation of absolute ethanol (can be judged by comparing with the original oil phase liquid level) Volatility), since the present embodiment prepares saturated saponified kerosene, the added solid sodium hydroxide is excessive, so the saponified product is filtered through 100 mesh filter paper to remove excess solid sodium hydroxide, and saturated saponified kerosene is obtained;

[0056] c. Take 1.2ml of saponified Cyanex272 and 8.8ml of satura...

Embodiment 3

[0064] The difference between this embodiment and embodiment 2 is only that the kerosene used to prepare the organic solvent is changed to sulfonated kerosene, and the others are the same as in embodiment 2.

[0065] Similarly, carry out ICP (inductively coupled plasma spectrometer / inductively coupled plasma emission spectrometer) detection to the aqueous phase of step f, the aqueous phase of g back-extraction gained, the water phase of h each back-extraction gained, determine wherein each element content , and the results are shown in Table 3.

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Abstract

The invention provides a lithium recovery and extraction method. The method mainly comprises the steps that sulfuric acid is used for soaking powder of matter to be recovered, obtained impregnation liquid is filtered, and the pH is adjusted; solid alkali metal hydroxide is utilized for preparing a saponification organic solvent; and the impregnation liquid is added into the saponification organicsolvent, oscillation is performed, and then a water phase is collected. According to the method, the solid alkali metal hydroxide is utilized for obtaining the saponification organic solvent (an oil phase), accordingly, a large amount of alkali metal matter exists in the oil phase, when the water phase impregnation liquid with a certain pH value is added into the oil phase, the oil phase can be used for extracting a large amount of other elements while the lithium element is kept in the water phase, an existing lithium element extraction operation process is simplified, in addition, producingof a large amount of precipitation of hydroxide is avoided, accordingly, output of sludge is controlled, a container is kept clean, and the aftertreatment load is greatly reduced; and in addition, theremnant oil phase after the lithium element is extracted can also be used for further separating other elements through acid pickling, elements are recycled as much as possible, and meanwhile, the oil phase can be recycled.

Description

technical field [0001] The invention relates to metal element recovery technology, in particular to a lithium element recovery and extraction method. Background technique [0002] With the improvement of environmental awareness and the threat of depletion of many resources, recycling technology is getting more and more attention. For example, batteries have become an indispensable consumer product in modern life, with an annual consumption of 8 billion, especially lithium-ion batteries. Due to its high energy density and fast charging speed, it has been developed rapidly and widely used, resulting in a large number of waste batteries that need to be disposed of urgently. For the recycling of batteries, especially the collection of various chemical components such as iron, cobalt, magnesium, manganese, nickel, zinc, lithium, etc., has attracted attention because it meets the needs of circular economy and green economy. Recovery methods include pyrometallurgy, hydrometallurgy...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B7/00C22B26/12
CPCC22B7/007C22B26/12Y02P10/20
Inventor 骆仲奕谢雅敏胡绍华骆仲品陈彦淇周信辉朱叶周
Owner 哈工(芜湖)新材料科技有限公司
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