Method for producing lithium-rich pure solution from waste lithium ion battery positive electrode active material

A positive electrode active material and lithium-ion battery technology, applied in battery recycling, waste collector recycling, recycling technology, etc., can solve the problems of low recovery rate, high energy consumption of lithium recovery, and large consumption of acid-base neutralization reagents, etc. Achieve the effect of high recovery rate of useful elements, reduce comprehensive recovery cost and increase recovery rate

Active Publication Date: 2018-11-06
BEIJING MINING & METALLURGICAL TECH GRP CO LTD
View PDF11 Cites 12 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

There are roughly two routes for the treatment of the leachate. One is to purify the leachate to remove harmful impurities such as iron and aluminum, and then directly precipitate to prepare the precursor of the positive electrode material. The precursor is returned to the battery company for utilization, and the precipitation method is used to produce the precursor. The process flow is short, but the product market is narrow, and the ingredients need to be adjusted to meet the production requirements of battery materials, and the consumption of acid-base neutralization reagents is large, and the precursors are washed repeatedly, resulting in a large amount of washing water and high sodium ions in the solution after precipitation , the concentration of lithium ions is low, resulting in high energy consumption for lithium recovery
Another solution is to purify the leaching solution to remove impurities such as iron and aluminum, then continue to extract and separate the purified solution to prepare nickel salt and cobalt salt, and recover lithium salt products from the raffinate after nickel and cobalt extraction. The lithium concentration in the raffinate is low and contains a large amount of sodium ions. To prepare lithium carbonate products, it is necessary to use evaporation and concentration for enrichment and then carbonate precipitation. Evaporation and concentration of low-concentration lithium salt solutions require high energy consumption. The sodium ion content in the residual liquid is high, resulting in the crystallization of a large amount of sodium salt and the entrainment loss of lithium salt during the concentration process, and resulting in high sodium content in subsequent lithium salt products, which require further purification to obtain battery-grade products
Moreover, the solubility product of lithium carbonate is large, the recovery rate of lithium carbonate precipitation is low, the lithium precipitation rate is less than 80%, and the lithium content after precipitation is still more than 2g / L
In addition, due to the use of a large amount of reducing agents such as hydrogen peroxide, which is expensive and difficult to transport and store during leaching, the cost of comprehensive utilization of waste lithium-ion battery cathode materials is high.
[0004] In addition, K, Na, Ca, and Mg are common impurities in the production of battery-grade lithium salts. Due to their similar chemical properties to Li, they are difficult to remove in the production of lithium salts, which is a difficult point in the study of lithium salt purification.

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Method for producing lithium-rich pure solution from waste lithium ion battery positive electrode active material

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] Take 200g of ternary battery positive electrode material containing 28.3% nickel, 10.63% cobalt, 11.75% manganese and 6.50% lithium, according to the acid ore mass ratio of 2:1, the hydrogen peroxide volume mass ratio of 1:1, the leaching solid-liquid mass-to-volume ratio 1:10, the leaching time is 1h for sulfuric acid reduction leaching; the leaching solution is adjusted by 30% NaOH solution to adjust the pH value to remove iron. Add sodium phosphate to the nickel extraction raffinate according to 1.2 times the theoretical amount of lithium moles. At 90°C, stir and react for 1 hour to obtain lithium-containing phosphate, the lithium precipitation rate is 96%, and the lithium-containing liquid contains 0.01 g / L; Lithium-containing phosphate concentrate is leached by 200g / L calcium chloride solution, leaching temperature is 90°C, leaching time is 2h, leaching solid-liquid mass to volume ratio is 1:8, lithium leaching rate is 98%, lithium-containing leaching solution The ...

Embodiment 2

[0027]Take 200g of ternary battery cathode material containing 28.3% nickel, 10.63% cobalt, 11.75% manganese and 6.50% lithium. The ratio of liquid mass to volume is 1:10, and the leaching time is 1h for leaching; the leaching liquid is leached through 30% NaOH solution to adjust the pH value to remove iron. Nickel extraction; add sodium phosphate to the nickel extraction raffinate according to 1.2 times the theoretical amount of lithium moles, stir and react for 1.5h at 90°C, the lithium precipitation rate is 96.5%, and the lithium-containing phosphate concentrate is obtained by solid-liquid separation , the lithium-containing phosphate concentrate was leached by 300g / L calcium chloride solution, the leaching temperature was 90°C, the leaching time was 1.5h, the leaching solid-liquid mass to volume ratio was 1:5, the lithium leaching rate was 98.5%, and the lithium-containing leaching solution contained lithium The concentration is about 22.5g / L.

Embodiment 3

[0029] Take 200g of ternary battery cathode material containing 28.3% nickel, 10.63% cobalt, 11.75% manganese and 6.50% lithium, mix the cathode material, concentrated sulfuric acid, and anthracite in proportion, wherein the amount of sulfuric acid added is based on the mass ratio of sulfuric acid to the cathode material 2: 1. The amount of anthracite added is 20% of the mass of the positive electrode material, the roasting temperature is 300°C, and the roasting time is 2 hours; the clinker is leached with water, the leached solid-liquid mass to volume ratio is 1:5, 1% hydrogen peroxide is added, the leaching time is 1 hour, nickel-cobalt The leaching rate of lithium is greater than 95%. The leaching solution adjusts the pH value with 30% NaOH solution to remove iron. Sodium phosphate is added to the solution according to 1.2 times the theoretical amount of lithium moles, and the reaction is stirred for 1 hour at 90°C, and the lithium precipitation rate is 95.5%. The concentra...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

No PUM Login to view more

Abstract

The invention discloses a method for producing a lithium-rich pure solution from a waste lithium ion battery positive electrode active material, belongs to the technical field of waste lithium ion battery material recycling, and particularly provides a method for producing a lithium-rich pure solution from a reduced sulfuric acid leaching solution of a positive electrode active material. A high-sodium and low-lithium lithium sulfate solution obtained after the positive electrode active material is subjected to reduction leaching and leaching solution purification is subjected to lithium deposition with phosphoric acid or phosphate to obtain lithium-containing phosphate enrichment; lithium is selectively leached out from the lithium-containing phosphate enrichment by using less than a theoretically required amount of a calcium chloride solution to obtain the lithium-rich pure solution and lithium-containing phosphorus-calcium residues; and the lithium-containing pure solution is used for producing a product such as battery-grade lithium carbonate or lithium chloride through a conventional method such as deposition or crystallization, and a solution obtained after the lithium-containing phosphorus-calcium residues are subjected to sulfuric acid leaching and neutralization returns to the lithium deposition step for cyclic use. According to the method, the lithium-rich pure solution can be directly produced from the high-sodium and low-lithium solution without pre-concentration, the energy consumption and the cost are low, and the lithium recycling rate is high.

Description

technical field [0001] The invention belongs to the technical field of recycling waste lithium ion battery materials, and in particular relates to a method for producing lithium-rich net liquid from the positive electrode active material of waste lithium ion batteries. Background technique [0002] Due to its high working voltage and specific energy, stable discharge voltage, light weight and small size, long cycle life, and no memory effect, lithium-ion batteries are widely used in portable devices, electric vehicles, power reserves, satellites and other fields. With the advancement of lithium-ion battery technology and the increase in output, its waste is also increasing year by year. The lifespan of lithium-ion batteries is generally 3 to 5 years. At present, the recycling system has not yet reached a large scale, and the recovery rate is low. Most of the waste lithium-ion batteries have not been effectively treated, which not only pollutes the environment, but also waste...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
Patent Type & Authority Applications(China)
IPC IPC(8): H01M10/54
CPCH01M10/54Y02W30/84
Inventor 蒋训雄李达刘巍汪胜东赵峰蒋伟
Owner BEIJING MINING & METALLURGICAL TECH GRP CO LTD
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products