Method for recovering lithium from waste lithium iron phosphate batteries and method for recovering lithium and iron phosphate

A lithium iron phosphate battery and lithium recovery technology, applied in the field of lithium ion batteries, can solve the problems of long overall process, complex process and high cost

Active Publication Date: 2020-09-18
NINGBO INST OF MATERIALS TECH & ENG CHINESE ACADEMY OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] In the above-mentioned prior art, when lithium is recovered, the recovery process is long, the concentration of lithium solution is low, and it is difficult to directly precipitate lithium to prepare lithium carbonate products. After obtaining lithium solution, it is necessary to carry out other treatments such as evaporation and concentration before proceeding to the subsequent preparation of lithium carbonate. The process is complicated, the cost is high, and the recycling effect is not good
In addition, in the prior art, when lithium and iron phosphate are recovered at the same time, the synthetic iron phosphate is recovered first, and then the remaining lithium-containing solution is processed to recover lithium. The overall process is long and the recovery effect is not good.

Method used

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  • Method for recovering lithium from waste lithium iron phosphate batteries and method for recovering lithium and iron phosphate
  • Method for recovering lithium from waste lithium iron phosphate batteries and method for recovering lithium and iron phosphate
  • Method for recovering lithium from waste lithium iron phosphate batteries and method for recovering lithium and iron phosphate

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Effect test

Embodiment 1

[0160] 1. Recycling and producing lithium carbonate from waste lithium iron phosphate batteries

[0161] a) Discharge, shred, and separate the waste lithium iron phosphate battery to obtain the shell, separator, and positive and negative electrodes; roast the positive and negative electrodes in a nitrogen atmosphere at 350°C, crush and sieve to obtain copper aluminum and positive and negative electrode powder . Among them, copper and aluminum are separated into copper powder and aluminum powder through variable-diameter dry separation columns for recycling. The positive and negative electrode powders and washing water were mixed at a solid-to-liquid ratio of 1:1 for slurrying, and reacted for 10 minutes to obtain slurrying liquid 1.

[0162] b) Add concentrated sulfuric acid (mass fraction: 98%) and hydrogen peroxide (concentration: 30%) to slurry mixing liquid 1, wherein, the amount of hydrogen peroxide added is 3 times of the theoretical amount, and concentrated sulfuric ac...

Embodiment 2

[0178] 1. Recycling and producing lithium carbonate from waste lithium iron phosphate batteries

[0179] a) Discharge, shred and separate the waste lithium iron phosphate battery to obtain the shell, diaphragm and positive and negative electrodes; roast the positive and negative electrodes at 600°C in a nitrogen atmosphere, crush and sieve to obtain copper aluminum and positive and negative electrode powder . Among them, copper and aluminum are separated into copper powder and aluminum powder through variable-diameter dry separation columns for recycling. The positive and negative electrode powders and washing water were mixed at a solid-to-liquid ratio of 1:2 for slurrying, and reacted for 10 minutes to obtain slurrying liquid 1.

[0180] b) Add concentrated sulfuric acid (mass fraction: 98%) and hydrogen peroxide (concentration: 30%) to slurrying liquid 1, wherein, the amount of hydrogen peroxide added is 1.2 times of the theoretical amount, and concentrated sulfuric acid i...

Embodiment 3

[0191] 1. Recycling and producing lithium carbonate from waste lithium iron phosphate batteries

[0192] a) Discharge, shred, and separate the waste lithium iron phosphate battery to obtain the casing, diaphragm, and positive and negative electrodes; roast the positive and negative electrodes at 450°C in a nitrogen atmosphere, and then pulverize and sieve to obtain copper aluminum and positive and negative electrode powders . Among them, copper and aluminum are separated into copper powder and aluminum powder through variable-diameter dry separation columns for recycling. The positive and negative electrode powders and washing water were mixed at a solid-to-liquid ratio of 1:1.5 for slurrying, and reacted for 10 minutes to obtain slurrying liquid 1.

[0193] b) Add concentrated sulfuric acid (mass fraction: 98%) and hydrogen peroxide (concentration: 30%) to slurry mixing liquid 1, wherein, the amount of hydrogen peroxide added is 2 times of the theoretical amount, and concent...

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Abstract

The invention provides a method for recovering lithium from waste lithium iron phosphate batteries, and a method for recovering lithium and iron phosphate. According to the method for recycling lithium, waste lithium iron phosphate batteries are pretreated to obtain positive and negative electrode powder, the positive and negative electrode powder reacts with water, concentrated sulfuric acid andammonia water to form a lithium-containing solution and iron-phosphorus slag, and the lithium-containing solution and the iron-phosphorus slag are separated through solid-liquid separation to obtain primary leachate and carbon-containing iron-phosphorus slag; the positive and negative electrode powder reacts with the primary leachate, concentrated sulfuric acid and ammonia water, and solid-liquidseparation is performed to obtain secondary leachate and carbon-containing iron-phosphorus slag; and an alkali is added into the obtained secondary leachate to adjust the pH value, solid-liquid separation is performed to remove impurities such as iron, aluminum and the like to obtain an impurity-removed solution, and the impurity-removed solution directly reacts with sodium carbonate to form a lithium carbonate product. According to the method, the recovery process can be simplified, the concentration of lithium in the lithium-containing solution is increased, lithium can be precipitated to generate lithium carbonate without evaporation and concentration, and the recovery rate is high; and the lithium carbonate product meets the industrial standard of lithium carbonate for batteries.

Description

technical field [0001] The invention relates to the field of lithium ion batteries, in particular to a method for recovering lithium from waste lithium iron phosphate batteries, and a method for recovering lithium and iron phosphate. Background technique [0002] Lithium iron phosphate power battery has stable chemical properties, good safety performance and long service life. At the same time, due to the low price of raw materials, it still occupies half of the power battery. In recent years, it has been widely used in various electric vehicles and energy storage fields. Behind the mass production and application means that a large number of waste lithium iron phosphate batteries are produced every year. According to the China Automobile Association's new energy vehicle production and sales data, the market inventory of lithium iron phosphate batteries is calculated, and it is estimated that the retired lithium iron phosphate batteries in 2020 will be 20.31GWh, 184,700 tons...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B25/37C01D15/08C22B7/00C22B26/12H01M10/0525H01M10/54
CPCC01B25/375C01D15/08H01M10/0525H01M10/54C22B7/007C22B26/12C01P2002/72C01P2006/80C01P2004/61C01P2006/10C01P2006/11C01P2006/82Y02E60/10Y02W30/84Y02P10/20
Inventor 高洁夏永高
Owner NINGBO INST OF MATERIALS TECH & ENG CHINESE ACADEMY OF SCI
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