CN101921917A - Method for reclaiming valuable metals from waste lithium batteries - Google Patents
Method for reclaiming valuable metals from waste lithium batteries Download PDFInfo
- Publication number
- CN101921917A CN101921917A CN2010102621982A CN201010262198A CN101921917A CN 101921917 A CN101921917 A CN 101921917A CN 2010102621982 A CN2010102621982 A CN 2010102621982A CN 201010262198 A CN201010262198 A CN 201010262198A CN 101921917 A CN101921917 A CN 101921917A
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- China
- Prior art keywords
- copper
- cobalt
- waste lithium
- lithium cell
- valuable metal
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/84—Recycling of batteries or fuel cells
Abstract
The invention discloses a method for reclaiming valuable metals from waste lithium batteries, which comprises the following steps of: crushing discharged waste lithium batteries, calcining at the high temperature of 350-400 DEG C to obtain a material containing cobalt, copper and aluminum, adding 5-10% sodium hydroxide solution to the material, making the sodium hydroxide solution react with the material for 2-3 hours, filtering alkaline liquor, washing and drying to obtain a material containing cobalt and copper; adding sulfuric acid with a certain concentration and Na2S2O3 to the material containing cobalt and copper, mixing, dissolving, adding an extractant to extract copper, and adding an extractant to the copper-extracted solution to extract cobalt. The method is simple and effective and has low reclamation cost.
Description
Technical field
The present invention relates to recycling, particularly from waste lithium cell, reclaim the method for valuable metal from waste lithium cell.
Background technology
Lithium ion battery has been widely used in the portable type electronic product field since 20th century, entered commercialization the nineties.But lithium ion battery is after using after a while, and electrode materials can expand, shrink, even the performance of active substance also will change, and cause the decline of cell container, even battery is scrapped.In recent years, along with lithium ion battery applications more and more widely, the battery consumption increases rapidly, the lithium ion battery of scrapping also will increase year by year significantly.After the lithium ion battery of these tons oves is scrapped, can produce serious potential safety hazard and environmental pollution if deal with improperly, also can cause the great wasting of resources simultaneously, along with the positive development of society and the people pay attention to day by day to environmental protection, the recovery of waste and old lithium ion battery will become very urgent problem.
Contain the multiple precious metal that recovery value is arranged in the lithium ion battery, as cobalt, copper, lithium, aluminium etc., therefore, the recycling lithium ion battery has bigger economic worth, but at present also not simply, recovery and treatment method efficiently.
Summary of the invention
At above-mentioned technological deficiency, the invention discloses a kind of method that from waste lithium cell, reclaims valuable metal, this method is simple, efficient, cost is low.
Technical scheme of the present invention is as described below: a kind of method from waste lithium cell recovery valuable metal, comprise the steps,
(1) the waste lithium cell mechanical disintegration after will discharging;
(2) 350 ℃ of-400 ℃ of calcinings of high temperature obtain containing the material of cobalt, copper and aluminium;
(3) adding content is the sodium hydroxide solution of 5%-10%, reacts 2-3 hour, alkali lye is filtered, and washing, drying obtains containing the material of cobalt, copper;
(4) material that contains cobalt, copper is added certain density sulfuric acid and Na
2s
2O
3,Stirring and dissolving adds the extraction agent extracting copper;
(5) solution behind the extracting copper is added extraction agent extraction cobalt.
Alkali lye to after filtering in the step (3) adds dilute sulphuric acid, and adjusting pH is 8.5-9.0, precipitates 30-40 minute 90-100 ℃ of following ageing, filters and obtains aluminum hydroxide crystals.
Vitriolic concentration is 3.5 mol/L-4.0mol/L in the described step (4), Na
2s
2O
3Concentration be 0.3 mol/L-0.4mol/L.
Regulating the pH value in the described step (4) is 1.0, with the extraction agent extracting copper that contains 10%-15%Acorga M5640.
Regulator solution pH value is 5.0-5.5 in the described step (5), with the organic extractant extraction cobalt that contains 15%-20%Cyanex272.
Beneficial effect of the present invention is: the method from waste lithium cell recovery valuable metal of the present invention is simple, and the cost recovery of aluminium, copper, cobalt metal is low, the organic efficiency height.
Embodiment
To describe the present invention by embodiment below.
Embodiment 1:
With the waste lithium cell mechanical disintegration after the discharge, 350 ℃ of-400 ℃ of calcinings of high temperature, obtain containing the material of cobalt, copper and aluminium, adding content is 10% sodium hydroxide solution, reacted 2 hours, alkali lye is filtered, washing, drying obtains containing the material of cobalt, copper, and it is sulfuric acid and the 0.4mol/L Na of 3.5 mol/L that the material that contains cobalt, copper is added concentration
2s
2O
3,Stirring and dissolving, regulating pH value is 1.0, with the extraction agent extracting copper that contains 10%Acorga M5640, is 5.0-5.5 to the solution regulator solution pH value behind the extracting copper, usefulness contains the organic extractant extraction cobalt of 15% Cyanex272.Wherein to the alkali lye after filtering, add dilute sulphuric acid, adjusting pH is 8.5-9.0, precipitates 30-40 minute 90-100 ℃ of following ageing, filters and obtains aluminum hydroxide crystals.
Embodiment 2:
With the waste lithium cell mechanical disintegration after the discharge, 350 ℃ of-400 ℃ of calcinings of high temperature, obtain containing the material of cobalt, copper and aluminium, adding content is 10% sodium hydroxide solution, reacted 2 hours, alkali lye is filtered, washing, drying obtains containing the material of cobalt, copper, and it is sulfuric acid and the 0.35mol/L Na of 4.0mol/L that the material that contains cobalt, copper is added concentration
2s
2O
3,Stirring and dissolving, regulating the pH value is 1.0, with the extraction agent extracting copper that contains 15%Acorga M5640, is 5.0-5.5 to the solution regulator solution pH value behind the extracting copper, with the organic extractant extraction cobalt that contains 120%Cyanex272.Wherein to the alkali lye after filtering, add dilute sulphuric acid, adjusting pH is 8.5-9.0, precipitates 30-40 minute 90-100 ℃ of following ageing, filters and obtains aluminum hydroxide crystals.
Embodiment 3:
With the waste lithium cell mechanical disintegration after the discharge, 350 ℃ of-400 ℃ of calcinings of high temperature, obtain containing the material of cobalt, copper and aluminium, adding content is 15% sodium hydroxide solution, reacted 2 hours, alkali lye is filtered, washing, drying obtains containing the material of cobalt, copper, and it is sulfuric acid and the 0.4mol/L Na of 4.0mol/L that the material that contains cobalt, copper is added concentration
2s
2O
3,Stirring and dissolving, regulating the pH value is 1.0, with the extraction agent extracting copper that contains 12%Acorga M5640, is 5.0-5.5 to the solution regulator solution pH value behind the extracting copper, with the organic extractant extraction cobalt that contains 16%Cyanex272.Wherein to the alkali lye after filtering, add dilute sulphuric acid, adjusting pH is 8.5-9.0, precipitates 30-40 minute 90-100 ℃ of following ageing, filters and obtains aluminum hydroxide crystals.
The above only is preferred embodiment of the present invention, and all equalizations of being done according to claim scope of the present invention change and modify, and all should belong to the covering scope of claim of the present invention.
Claims (5)
1. one kind is reclaimed the method for valuable metal from waste lithium cell, it is characterized in that: comprise the steps,
(1) the waste lithium cell mechanical disintegration after will discharging;
(2) 350 ℃ of-400 ℃ of calcinings of high temperature obtain containing the material of cobalt, copper and aluminium;
(3) adding content is the sodium hydroxide solution of 5%-10%, reacts 2-3 hour, alkali lye is filtered, and washing, drying obtains containing the material of cobalt, copper;
(4) material that contains cobalt, copper is added certain density sulfuric acid and Na
2s
2O
3,Stirring and dissolving adds the extraction agent extracting copper;
(5) solution behind the extracting copper is added extraction agent extraction cobalt.
2. the method that reclaims valuable metal from waste lithium cell as claimed in claim 1, it is characterized in that: the alkali lye to after filtering in the step (3), add dilute sulphuric acid, adjusting pH is 8.5-9.0, precipitate 30-40 minute 90-100 ℃ of following ageing, filter and obtain aluminum hydroxide crystals.
3. waste lithium cell as claimed in claim 1 reclaims the method for valuable metal, it is characterized in that: vitriolic concentration is 3.5 mol/L-4.0mol/L in the described step (4), Na
2s
2O
3Concentration be 0.3 mol/L-0.4mol/L.
4. waste lithium cell as claimed in claim 3 reclaims the method for valuable metal, it is characterized in that: regulating the pH value in the described step (4) is 1.0, with the extraction agent extracting copper that contains 10%-15%Acorga M5640.
5. waste lithium cell as claimed in claim 1 reclaims the method for valuable metal, it is characterized in that: regulator solution pH value is 5.0-5.5 in the described step (5), with the organic extractant extraction cobalt that contains 15%-20%Cyanex272.
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CN2010102621982A CN101921917B (en) | 2010-08-25 | 2010-08-25 | Method for reclaiming valuable metals from waste lithium batteries |
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CN101921917B CN101921917B (en) | 2012-06-27 |
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102162034A (en) * | 2011-04-07 | 2011-08-24 | 常州今创博凡能源新材料有限公司 | Process for recovering valuable metals from waste lithium batteries |
CN102925697A (en) * | 2012-10-30 | 2013-02-13 | 南通博远合金铸件有限公司 | Production technology for recovering copper oxide from waste lithium battery |
CN105907989A (en) * | 2016-07-08 | 2016-08-31 | 长沙理工大学 | Method for recycling cobalt and lithium from waste lithium ion battery material |
CN108470956A (en) * | 2018-05-10 | 2018-08-31 | 天津聚雅源科技有限公司 | Chemical method disposes waste lithium cell system and waste lithium battery treatment |
CN109487083A (en) * | 2018-11-16 | 2019-03-19 | 江苏雄风科技有限公司 | A method of from liquid separating and recovering cobalt copper after the P204 back extraction in cobalt copper mine wet method smelting process |
CN110273068A (en) * | 2019-07-05 | 2019-09-24 | 武汉理工大学 | The method of recovering copper and cobalt in waste and old solid oxide fuel cell |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1536706A (en) * | 2003-04-04 | 2004-10-13 | 秦文隆 | Waste cell treatment method by using it as resource |
CN101555030A (en) * | 2009-05-04 | 2009-10-14 | 佛山市邦普镍钴技术有限公司 | Method for recovering and recycling waste lithium ion battery cathode material |
CN101707269A (en) * | 2009-10-14 | 2010-05-12 | 东莞新能源科技有限公司 | Method for recycling anode material of lithium ion battery |
-
2010
- 2010-08-25 CN CN2010102621982A patent/CN101921917B/en active Active
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1536706A (en) * | 2003-04-04 | 2004-10-13 | 秦文隆 | Waste cell treatment method by using it as resource |
CN101555030A (en) * | 2009-05-04 | 2009-10-14 | 佛山市邦普镍钴技术有限公司 | Method for recovering and recycling waste lithium ion battery cathode material |
CN101707269A (en) * | 2009-10-14 | 2010-05-12 | 东莞新能源科技有限公司 | Method for recycling anode material of lithium ion battery |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102162034A (en) * | 2011-04-07 | 2011-08-24 | 常州今创博凡能源新材料有限公司 | Process for recovering valuable metals from waste lithium batteries |
CN102925697A (en) * | 2012-10-30 | 2013-02-13 | 南通博远合金铸件有限公司 | Production technology for recovering copper oxide from waste lithium battery |
CN105907989A (en) * | 2016-07-08 | 2016-08-31 | 长沙理工大学 | Method for recycling cobalt and lithium from waste lithium ion battery material |
CN105907989B (en) * | 2016-07-08 | 2017-11-10 | 长沙理工大学 | A kind of method of Call Provision and lithium in material from used Li ion cell |
CN108470956A (en) * | 2018-05-10 | 2018-08-31 | 天津聚雅源科技有限公司 | Chemical method disposes waste lithium cell system and waste lithium battery treatment |
CN108470956B (en) * | 2018-05-10 | 2024-01-30 | 河南中天纳新科技有限公司 | System for disposing waste lithium battery by chemical method and waste lithium battery disposal method |
CN109487083A (en) * | 2018-11-16 | 2019-03-19 | 江苏雄风科技有限公司 | A method of from liquid separating and recovering cobalt copper after the P204 back extraction in cobalt copper mine wet method smelting process |
CN110273068A (en) * | 2019-07-05 | 2019-09-24 | 武汉理工大学 | The method of recovering copper and cobalt in waste and old solid oxide fuel cell |
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Effective date of registration: 20160726 Address after: 518000 Guangdong city of Shenzhen province Qianhai Shenzhen Hong Kong cooperation zone before Bay Road No. 1 building 201 room A Patentee after: Qianhai Shenzhen Jixiang Environmental Protection Technology Co., Ltd. Address before: 518000, Shenzhen, Guangdong, Nanshan District, Ma family Arts Dragon Road, Huijin homes 7 units 3C Patentee before: Shenzhen Tele Disused Battery Recycle Technology Co., Ltd. |