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Comprehensive recovery method of waste sodium-ion battery

A technology of sodium-ion batteries and recycling methods, which is applied in the field of comprehensive recycling of waste sodium-ion batteries, and can solve problems such as environmental threats, increased battery recycling costs, and secondary pollution

Pending Publication Date: 2022-03-25
GUANGDONG BRUNP RECYCLING TECH +2
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In the hydrometallurgical process, on the one hand, based on the principle of thermodynamics, reducing agents such as hydrogen peroxide, starch, and glucose are generally added to the wet leaching system. Although the addition of reducing agents can effectively increase the reaction temperature and leaching efficiency, the acid leaching The system will inevitably be affected, and it is easy to cause secondary pollution, such as the production of toxic gas acid gas (Cl 2 , SO 2 , NO x ), organic wastewater and thus poses a threat to the environment
On the other hand, carbonaceous materials (such as carbon-based negative electrode materials, conductive agents, binders, separators) can convert waste battery positive electrode materials into metal elements or metal oxides, and a considerable part of carbonaceous materials will inevitably remain. Reduction of roasted waste metals in roasting will lead to the complexity of subsequent separation and excessive use of chemical reagents for leaching, reducing the recovery rate and the efficiency and purity of valuable metals obtained, which will also further increase the recycling cost of batteries and reduce the target Quality of products

Method used

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  • Comprehensive recovery method of waste sodium-ion battery
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  • Comprehensive recovery method of waste sodium-ion battery

Examples

Experimental program
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Effect test

Embodiment 1

[0036] A comprehensive recovery method for waste sodium ion batteries, the specific process is:

[0037] (1) Pretreatment of waste sodium-ion batteries: Disassemble the shell of waste sodium-ion batteries, soak and discharge waste sodium-ion batteries in 0.13wt% sodium chloride, place in a sintering furnace at a temperature of 155°C, and evaporate the internal electrolyte of the battery for 3 hours and 36 minutes. Crushing, using a multi-stage vibrating sieve to sieve out the battery case and aluminum foil current collector, and the under-sieve is battery black powder;

[0038] (2) Battery black powder leaching treatment: 150g of black powder and 12g of sodium carbonate were mixed and ground for 54 minutes, 80mL of 0.54mol / L sodium sulfite and 1.5L of 3.27mol / L ammonia liquid were added, leached at 53°C, and solid-liquid separation was obtained The leaching solution and solid are dissolved by adding dilute sulfuric acid with a concentration of 0.21 mol / L to the solid, and the ...

Embodiment 2

[0041] A comprehensive recovery method for waste sodium ion batteries, the specific process is:

[0042] (1) Pretreatment of waste sodium-ion batteries: Disassemble the shell of waste sodium-ion batteries, soak and discharge waste sodium-ion batteries in 0.13wt% sodium chloride, place in a sintering furnace at a temperature of 155°C, and evaporate the internal electrolyte of the battery for 3 hours and 36 minutes. Crushing, using a multi-stage vibrating sieve to sieve out the battery case and aluminum foil current collector, and the under-sieve is battery black powder;

[0043] (2) Battery black powder leaching treatment: 150g of black powder and 7.5g of sodium carbonate were mixed and ground for 69 minutes, 60mL of 0.54mol / L sodium sulfite and 1.2L of 3.27mol / L ammonia liquid were added, leached at 53°C, and solid-liquid separation Obtain leaching solution and solid, dissolve the solid with dilute sulfuric acid with a concentration of 0.21mol / L, separate the carbon residue, s...

Embodiment 3

[0046] A comprehensive recovery method for waste sodium ion batteries, the specific process is:

[0047] (1) Pretreatment of waste sodium-ion batteries: Disassemble the casing of waste sodium-ion batteries, soak and discharge waste sodium-ion batteries in 0.04wt% sodium sulfate, place in a sintering furnace at a temperature of 185°C, evaporate the electrolyte inside the battery for 3h23min, and crush , Use a multi-stage vibrating sieve to sieve out the battery case and aluminum foil current collector, and the under-sieve is battery black powder;

[0048] (2) Battery black powder leaching treatment: 120g of black powder and 10g of ammonium sulfate were mixed and ground for 87 minutes, 75mL of 0.54mol / L sodium sulfite and 1.0L of 3.35mol / L ammonia liquid were added, leached at 64°C, and solid-liquid separation was obtained The leaching solution and solid are dissolved by adding dilute hydrochloric acid with a concentration of 0.46mol / L to dissolve the solid, and the carbon resid...

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PUM

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Abstract

The invention discloses a comprehensive recovery method of waste sodium-ion batteries, which comprises the following steps: mixing and grinding battery black powder and a pre-leaching agent, adding a reducing agent and ammonia liquor for leaching, carrying out solid-liquid separation to obtain a leachate and a solid, adding acid into the solid for dissolving, carrying out solid-liquid separation to obtain carbon residue and filtrate, adding alkali into the filtrate for adjusting pH, and separating to obtain aluminum hydroxide, alkali is continuously added into the filtrate to adjust the pH, manganese hydroxide is obtained through separation, a first oxidizing agent, a chelating agent and alkali are added into the leachate, ammonia distillation and solid-liquid separation are carried out, and a cobalt-containing insoluble substance and a nickel-containing chelate solution are obtained. According to the method, the battery black powder and the pre-leaching agent are subjected to ammonia leaching, Mn and Al in a reaction system are precipitated, Na, Ni and Co are still stored in the leaching agent, the separation and recovery difficulty of valuable metal compounds in the leaching agent can be reduced, the subsequent precipitation and separation procedures are greatly reduced, then a chelating agent and nickel are utilized for generating a chelate, nickel and cobalt in the solution coexist in the form of different substances, and the separation efficiency is improved. Therefore, high-efficiency separation of nickel and cobalt is realized.

Description

technical field [0001] The invention belongs to the technical field of battery recycling, and in particular relates to a comprehensive recycling method for waste sodium ion batteries. Background technique [0002] Waste sodium-ion batteries (NIBs) contain a large amount of valuable substances, such as sodium, manganese, nickel, cobalt, etc., which have serious impacts on the environment if not properly disposed of. Batteries become an important research aspect in the field of resource recycling. [0003] At present, the methods for recovering valuable metals from waste batteries can be roughly divided into direct regeneration, hydrometallurgy, and pyrometallurgy. The direct regeneration method includes hydrothermal regeneration and solid phase regeneration, both of which have strict requirements on the purity of waste positive and negative electrode materials, which limits its application in the treatment of waste batteries containing a large amount of impurities. Various ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01F7/34C01C1/02C01G45/02C01G51/04C01G53/00H01M10/054H01M10/54
CPCC01F7/34C01G45/02C01C1/024C01G51/04C01G53/00H01M10/54H01M10/054C01P2006/80Y02E60/10Y02W30/84Y02P10/20
Inventor 余海军张学梅谢英豪李爱霞钟应声李长东
Owner GUANGDONG BRUNP RECYCLING TECH
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