Method for recovering lithium from lithium iron phosphate waste and application thereof

A lithium iron phosphate and recycling method technology, applied in recycling technology, waste collector recycling, battery recycling, etc., can solve the problem that the recovery rate of lithium carbonate is difficult to guarantee, the performance of lithium iron phosphate material is affected, and phosphorus resource recycling is not considered. Consumption and other problems, to achieve the effect of low energy consumption cost, considerable economic benefits, and low equipment requirements

Active Publication Date: 2021-04-20
HUNAN BRUNP RECYCLING TECH +2
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In the related technology, lithium iron phosphate waste is re-prepared into lithium iron phosphate material by heat treatment-acid leaching-sinking iron phosphate-sinking lithium carbonate-lithium iron phosphate synthesis process, but due to the complexity of raw material components in this process, A large number of impurities (such as aluminum) will be included in iron phosphate, which will affect the performance of the synthesized lithium iron phosphate material, and the lithium recovery rate of lithium carbonate recovered by this method is difficult to guarantee
In the related technology, oxidation roasting-phosphoric acid leaching-liquid-solid separation-precipitation lithium carbonate process is used to achieve efficient separation of lithium and phosphorus iron, and the effect is good, but the recovery of phosphorus resources and the consumption of acid are not considered, and the cost is high
In the related art, waste lithium iron phosphate batteries are sorted to obtain lithium-containing positive electrode powder, a certain amount of acid is added to the lithium-containing powder to control the pH to 2.5-6.5, and lithium sulfate solution and iron phosphate precipitation are obtained. Lithium sulfate is used to prepare Lithium phosphate and iron phosphate precipitation are calcined to obtain iron orthophosphate. This method has a simple process and a high lithium recovery rate. However, this method still uses the traditional acid immersion wet process, which consumes acid and costs a lot.

Method used

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  • Method for recovering lithium from lithium iron phosphate waste and application thereof
  • Method for recovering lithium from lithium iron phosphate waste and application thereof
  • Method for recovering lithium from lithium iron phosphate waste and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0033] The recovery method of lithium in the lithium iron phosphate waste material of the present embodiment may further comprise the steps:

[0034] (1) 100g mass fraction of 96.8% lithium iron phosphate waste and 600ml pure water are mixed and pulped to obtain lithium iron phosphate slurry;

[0035] (2) Add 173 grams of ferric chloride to the slurry obtained in step (1), heat up to 50° C., react for 45 minutes, filter to obtain 700 ml of lithium chloride and ferrous chloride solution, and obtain 95.7 grams of ferric phosphate slag ;

[0036] (3) Feed oxygen into the solution containing lithium chloride and ferrous chloride obtained in step (2), react at 50° C. for 50 minutes, filter to obtain lithium chloride, ferric chloride solution and ferric hydroxide products;

[0037] (4) Lithium chloride, ferric chloride solution in step (3) and lithium iron phosphate battery powder in step (1) are subjected to 5 times of countercurrent cycle leaching, enriching lithium content while...

Embodiment 2

[0041] The recovery method of lithium in the lithium iron phosphate waste material of the present embodiment may further comprise the steps:

[0042] (1) 100g mass fraction of 96.8% lithium iron phosphate waste and 700ml pure water are mixed and pulped to obtain lithium iron phosphate slurry;

[0043] (2) Add 173 grams of ferric chloride to the slurry obtained in step (1), heat up to 40° C., react for 30 minutes, filter to obtain 800 ml of lithium chloride and ferrous chloride solution, and obtain 95.0 grams of ferric phosphate slag ;

[0044] (3) Pass into ozone to step (2) to obtain containing lithium chloride and ferrous chloride solution, at 50 ℃, reaction time 40min, filter and obtain lithium chloride, ferric chloride solution and ferric hydroxide product;

[0045] (4) Lithium chloride, ferric chloride solution in step (3) and lithium iron phosphate battery powder in step (1) are subjected to 10 countercurrent cycle leaching, enriching lithium content while reducing iron...

Embodiment 3

[0047] The recovery method of lithium in the lithium iron phosphate waste material of the present embodiment may further comprise the steps:

[0048] (1) 100g mass fraction of 96.8% lithium iron phosphate waste and 800ml pure water are mixed and pulped to obtain lithium iron phosphate slurry;

[0049] (2) Add 173 grams of ferric chloride to the slurry obtained in step (1), heat up to 60° C., react for 30 minutes, filter to obtain 900 ml of lithium chloride and ferrous chloride solution, and obtain 93.9 grams of ferric phosphate slag ;

[0050] (3) Pass through hydrogen peroxide to the solution containing lithium chloride and ferrous chloride obtained in step (2), react at 60° C. for 30 minutes, filter to obtain lithium chloride, ferric chloride solution and ferric hydroxide products;

[0051] (4) Lithium chloride, ferric chloride solution in step (3) and lithium iron phosphate battery powder in step (1) are subjected to 15 countercurrent cycle leaching, enriching lithium conten...

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Abstract

The invention belongs to the technical field of lithium ion battery material recovery, and discloses a method for recovering lithium from lithium iron phosphate waste and an application thereof, wherein the method comprises the following steps: (1) adding water into the lithium iron phosphate waste to prepare slurry to obtain lithium iron phosphate slurry; (2) adding soluble iron salt into the lithium iron phosphate slurry, reacting, and filtering to obtain filtrate containing Li<+> and Fe<2+> and iron phosphate slag; (3) adding an oxidizing agent into the filtrate, and filtering to obtain filtrate containing Li<+> and Fe<3+> and ferric hydroxide; and (4) carrying out multistage countercurrent circulation leaching on the filtrate and lithium iron phosphate battery powder to obtain a lithium solution. According to the method, the soluble ferric salt is adopted, the soluble ferric salt belongs to strong acid and weak base salt, the conversion of lithium iron phosphate can be accelerated, and the direct recovery rate of the primary conversion iron phosphate slag is about 98.5% and the direct recovery rate of lithium is about 98.5% by combining the oxidation of the oxidant.

Description

technical field [0001] The invention belongs to the technical field of lithium ion battery material recovery, and in particular relates to a method for recovering lithium from lithium iron phosphate waste and its application. Background technique [0002] Lithium iron phosphate is currently the most widely used lithium-ion battery material, and is regarded by many industry insiders as the future development direction of lithium batteries. Since the 21st century, with the blowout development of the lithium battery new energy market, the problem of disposing of waste lithium iron phosphate batteries has become increasingly prominent. [0003] At present, there are two recycling technologies for the positive electrode materials of waste lithium iron phosphate batteries: pyrometallurgy and hydrometallurgy. In terms of pyrometallurgy, the main method is to repair lithium iron phosphate to achieve secondary utilization. This method has complicated procedures, high energy consumpt...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B25/37C01G49/02C22B7/00C22B26/12H01M10/0525H01M10/54
CPCH01M10/0525H01M10/54C01B25/37C01G49/02C22B7/00C22B26/12Y02P10/20Y02W30/84
Inventor 郑显亮乔延超陈若葵谭枫孙颉李长东
Owner HUNAN BRUNP RECYCLING TECH
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