CN103757221A - Method for leaching positive pole material of waste lithium nickelate battery - Google Patents
Method for leaching positive pole material of waste lithium nickelate battery Download PDFInfo
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- CN103757221A CN103757221A CN201310736440.9A CN201310736440A CN103757221A CN 103757221 A CN103757221 A CN 103757221A CN 201310736440 A CN201310736440 A CN 201310736440A CN 103757221 A CN103757221 A CN 103757221A
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- leaching
- battery
- sulfuric acid
- nitric acid
- acid
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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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Abstract
The invention discloses a method for leaching a positive pole material of a waste lithium nickelate battery. The method comprises the steps of adding the positive pole material which is separated from the waste lithium nickelate battery and is subjected to roasting pretreatment, and napier grass powder into a reaction kettle which is resistant to pressure and the corrosion of sulfuric acid and nitric acid, adding a mixed solution of sulfuric acid and nitric acid, and leaching while stirring under closed conditions.
Description
Technical field
The present invention relates to a kind of leaching method of anode material of waste LiNiO 2 battery.
Background technology
Lithium nickelate battery is the widely used battery of a class, and this battery will produce a large amount of refuse batteries after using and scrapping.Because this class battery contains plurality of heavy metal, if abandon into environment, will environment be produced to very large direct and potential hazard.Anode material of waste LiNiO 2 battery is nickeliferous, lithium, copper and aluminium mainly, and wherein nickel, lithium and copper three's total content is greater than 60%, has very much a recovery value.The technique that reclaims at present nickel, lithium and copper from anode material of waste LiNiO 2 battery mainly contains thermal process and wet processing.The product that thermal process obtains is alloy material, nickel, lithium and copper that very difficult acquisition is purer.Wet processing becomes more readily available purer nickel, lithium and copper.Leaching is a requisite process in wet processing.The leaching method of anode material of waste LiNiO 2 battery mainly contains hydrochloric acid leaching process, sulfuric acid leaching, nitric acid lixiviation process and nitration mixture (sulfuric acid adds nitric acid) lixiviation process at present.Hydrochloric acid leaching process, equipment corrosion is large, the large and contaminate environment of acid mist generation.The more expensive reductive agent of sulfuric acid leaching consumption (as hydrogen peroxide etc.), and leaching velocity is slower, and acid consumption is high.The nitric acid consumption of nitric acid lixiviation process is large, and can produce a large amount of oxynitride, contaminate environment.All there is the problem that improves how economically leaching velocity, raising metal leaching rate, reduces acid consumption and other supplementary product onsumption in all wet processings.Although nitric acid processing industry pure oxygen lixiviation process and nitration mixture processing industry pure oxygen lixiviation process have solved the problems referred to above preferably, but leaching plant is more complicated, and the required industrial pure oxygen amount of refuse battery leaching is little, refuse battery is processed enterprise, and manufacture pure oxygen is personal uneconomical on the spot, and storage, transportation and the use of industrial pure oxygen are cumbersome.Development equipment corrosion is little, leaching velocity is fast, leaching yield is high, acid consumes and other supplementary product onsumption is low, easy to use, the leaching method of the anode material of waste LiNiO 2 battery of basic non-environmental-pollution has larger practical value.
Summary of the invention
The problem leaching for current anode material of waste LiNiO 2 battery, the object of the invention is to find a kind of metal leaching rate high, leaching velocity is fast, leaching yield is high, acid consumption and other supplementary product onsumption are low, easy to use, need not expensive reductive agent, the leaching method of the anode material of waste LiNiO 2 battery of basic non-environmental-pollution, it is characterized in that by positive electrode material isolated from waste LiNiO 2 battery and that obtain through roasting pretreatment and≤the napier grass powder of 1.5mm adds withstand voltage, in the reactor of resistance to sulfuric acid and nitric acid corrosion, add the mixing solutions of sulfuric acid and nitric acid, and carry out in confined conditions agitation leach.After leaching finishes, carry out liquid-solid separation, obtain required infusion solution.Temperature of reaction is 60 ℃~80 ℃, and the sulfuric acid starting point concentration of leaching is 1mol/L~4mol/L, and the starting point concentration of nitric acid is that 5g/L~10g/L extraction time is 2h~4h, and leaching process stirs, and stirring velocity is 30r/min~120r/min.Sulphuric acid is to add 110%~140% of sulfuric acid theoretical consumption that in the positive electrode material of reaction vessel, all metals leach.The add-on of napier grass powder is counted LiNiO in positive electrode material with butt
290%~120% of quality.
The object of the present invention is achieved like this: airtight and have under the condition that napier grass powder and nitric acid exists, (nickel in material and lithium exist with lithium nickelate form the anode material of waste LiNiO 2 battery of sulfuric acid leaching after roasting pretreatment, copper and aluminium are mainly metal oxide form) time, there is following main chemical reactions in leaching process:
CuO?+?H
2SO
4?=?CuSO
4?+?H
2O
Al
2O
3?+?3H
2SO
4?=?3Al
2(SO
4)
3?+?3H
2O
nC
6H
10O
5?+?nH
2SO
4?=n(C
5H
11O
5)HSO
4
n(C
5H
11O
5)HSO
4?+?nH
2O?=?nC
6H
12O
6?+?nH
2SO
4
C
6H
12O
6?+?8HNO
3?=?8NO?+?6CO
2?+?10H
2O
nC
6H
10O
5?+?8nHNO
3?=?8nNO?+?6nCO
2?+?9nH
2O
6LiNiO
2?+?9H
2SO
4?+?2NO?=?6NiSO
4?+?3Li
2SO
4?+?2HNO
3?+?8H
2O
The total reaction of lithium nickelate is:
24nLiNiO
2?+?nC
6H
10O
5?+?36nH
2SO
4?=?24nNiSO
4?+?12nLi
2SO
4?+?6nCO
2?+?41nH
2O
Other organism in napier grass powder also generates NO, CO with nitric acid reaction
2and H
2o, the NO of generation and LiNiO
2and H
2sO
4by previous reaction, generate NiSO
4, Li
2sO
4, HNO
3and H
2o.
Because the speed of response of nitric acid and napier grass powder is very fast, the NO of generation and LiNiO
2reaction also very fast, accelerate thus whole leaching process, and realize LiNiO
2leach more completely.NO can thoroughly destroy the laminate structure of high oxide in positive electrode material, improves the leaching yield of valuable metal.
With respect to existing method, outstanding advantages of the present invention is to adopt napier grass powder to make reductive agent, and nitric acid is made to leach accelerator and leached anode material of waste LiNiO 2 battery, and speed of response is fast, and such as reaction acidity is lower, and the consumption of sulfuric acid and reductive agent is little, and napier grass powder is cheap; In positive electrode material, the laminate structure of high oxide is destroyed thoroughly, can improve metal leaching rate; In leach liquor subsequent disposal, do not need to neutralize a large amount of acid, cost is lower; The waste amount producing in leach liquor subsequent disposal is few, has reduced pollution abatement costs, has obvious economic benefit and environmental benefit; Process is carried out in confined conditions, the environmental pollution of having avoided NO effusion to produce.
specific implementation method
embodiment 1: by 100g anode material of waste LiNiO 2 battery (nickeliferous 54.3%, lithium 5.5%, copper 7.8%, aluminium 3.1%) and≤to add volume be in the lining titanium pressure reaction still of 2L to 1.5mm napier grass powder 30g, adding sulfuric acid concentration is the mixed acid solution 1300ml that 1.5mol/L, concentration of nitric acid are 5g/L, at 60 ℃~70 ℃, stir (stirring velocity 80r/min) and leach 4.0h, after leaching finishes, carry out liquid-solid separation, obtain 1250ml infusion solution (not containing leached mud washing water).The leaching yield of nickel, lithium, copper and aluminium be respectively 99.2%, 99.4%, 98.3% and 98.4%(by entering nickel in infusion solution and leached mud washings, lithium, copper and aluminium, calculate).
Embodiment 2: by 500g anode material of waste LiNiO 2 battery (nickeliferous 54.3%, lithium 5.5%, copper 7.8%, aluminium 3.1%) to add volume be in the lining titanium pressure reaction still of 5L to≤1.5mm napier grass powder 190g, add mixed acid solution 3200 ml that sulfuric acid concentration 3.5mol/L, concentration of nitric acid are 10g/L, at 70 ℃~80 ℃, stir (stirring velocity 70r/min) and leach 2.0h, after leaching finishes, carry out liquid-solid separation, obtain 3000 ml infusion solutions (not containing leached mud washing water).The leaching yield of nickel, lithium, copper and aluminium be respectively 99.2%, 99.5%, 99.1% and 98.8%(by entering nickel in infusion solution and leached mud washings, lithium, copper and aluminium, calculate).
Claims (1)
1. the leaching method of an anode material of waste LiNiO 2 battery, it is characterized in that by positive electrode material isolated from waste LiNiO 2 battery and that obtain through roasting pretreatment and≤the napier grass powder of 1.5mm adds withstand voltage, in the reactor of resistance to sulfuric acid and nitric acid corrosion, add the mixing solutions of sulfuric acid and nitric acid, and carry out in confined conditions agitation leach, after finishing, leaching carries out liquid-solid separation, obtain required infusion solution, temperature of reaction is 60 ℃~80 ℃, the sulfuric acid starting point concentration leaching is 1mol/L~4mol/L, the starting point concentration of nitric acid is that 5g/L~10g/L extraction time is 2h~4h, leaching process stirs, stirring velocity is 30r/min~120r/min, sulphuric acid is to add 101%~140% of sulfuric acid theoretical consumption that in the positive electrode material of reaction vessel, all metals leach, the add-on of napier grass powder is counted LiNiO in positive electrode material with butt
290%~120% of quality.
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CN201310736440.9A CN103757221A (en) | 2013-12-29 | 2013-12-29 | Method for leaching positive pole material of waste lithium nickelate battery |
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---|---|---|---|
CN201310736440.9A CN103757221A (en) | 2013-12-29 | 2013-12-29 | Method for leaching positive pole material of waste lithium nickelate battery |
Publications (1)
Publication Number | Publication Date |
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CN103757221A true CN103757221A (en) | 2014-04-30 |
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ID=50524535
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CN201310736440.9A Pending CN103757221A (en) | 2013-12-29 | 2013-12-29 | Method for leaching positive pole material of waste lithium nickelate battery |
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Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101619394A (en) * | 2009-06-23 | 2010-01-06 | 四川师范大学 | Method for leaching anode and cathode mixed material of waste lithium nickel manganese cobalt battery |
CN102030375A (en) * | 2010-10-29 | 2011-04-27 | 北京矿冶研究总院 | Method for preparing lithium cobaltate by directly using failed lithium ion battery |
-
2013
- 2013-12-29 CN CN201310736440.9A patent/CN103757221A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101619394A (en) * | 2009-06-23 | 2010-01-06 | 四川师范大学 | Method for leaching anode and cathode mixed material of waste lithium nickel manganese cobalt battery |
CN102030375A (en) * | 2010-10-29 | 2011-04-27 | 北京矿冶研究总院 | Method for preparing lithium cobaltate by directly using failed lithium ion battery |
Non-Patent Citations (1)
Title |
---|
李进中,钟宏: "氧化锰矿还原浸出工艺技术研究进展", 《中国锰业》 * |
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Application publication date: 20140430 |