Nothing Special   »   [go: up one dir, main page]

CN103199320B - Method for recycling nickel-cobalt-manganese ternary anode material - Google Patents

Method for recycling nickel-cobalt-manganese ternary anode material Download PDF

Info

Publication number
CN103199320B
CN103199320B CN201310104022.8A CN201310104022A CN103199320B CN 103199320 B CN103199320 B CN 103199320B CN 201310104022 A CN201310104022 A CN 201310104022A CN 103199320 B CN103199320 B CN 103199320B
Authority
CN
China
Prior art keywords
cobalt
nickel
manganese
lithium
anode material
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201310104022.8A
Other languages
Chinese (zh)
Other versions
CN103199320A (en
Inventor
熊仁利
王平
黄春莲
严新星
王梓丞
何霞
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tianqi lithium industry (Jiangsu) Co., Ltd.
Tianqi Lithium Industry (Shehong) Co., Ltd.
Tianqi Lithium Industry Co., Ltd.
Original Assignee
Sichuan Tianqi Lithium Industriesinc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sichuan Tianqi Lithium Industriesinc filed Critical Sichuan Tianqi Lithium Industriesinc
Priority to CN201310104022.8A priority Critical patent/CN103199320B/en
Publication of CN103199320A publication Critical patent/CN103199320A/en
Priority to PCT/CN2014/074157 priority patent/WO2014154152A1/en
Application granted granted Critical
Publication of CN103199320B publication Critical patent/CN103199320B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G53/00Compounds of nickel
    • C01G53/40Nickelates
    • C01G53/42Nickelates containing alkali metals, e.g. LiNiO2
    • C01G53/44Nickelates containing alkali metals, e.g. LiNiO2 containing manganese
    • C01G53/50Nickelates containing alkali metals, e.g. LiNiO2 containing manganese of the type [MnO2]n-, e.g. Li(NixMn1-x)O2, Li(MyNixMn1-x-y)O2
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G53/00Compounds of nickel
    • C01G53/006Compounds containing, besides nickel, two or more other elements, with the exception of oxygen or hydrogen
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2004/00Particle morphology
    • C01P2004/60Particles characterised by their size
    • C01P2004/61Micrometer sized, i.e. from 1-100 micrometer
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/54Reclaiming serviceable parts of waste accumulators
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/84Recycling of batteries or fuel cells

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Secondary Cells (AREA)

Abstract

The invention relates to a method for recycling a nickel-cobalt-manganese ternary anode material, belongs to the technical field of recovery of waste cells, and solves the technical problem that a method for recycling the nickel-cobalt-manganese ternary anode material is provided. The method for recycling the nickel-cobalt-manganese ternary anode material comprises a step of removing a binder from the positiveplate of the nickel-cobalt-manganese ternary material by thermal treatment, and the method for removing the binder in the positive plate of the nickel-cobalt-manganese ternary material is thermal treatment of the positive plate of the nickel-cobalt-manganese ternary anode material at 400-1000 DEG C for 0.5-5 hours.

Description

The method that nickel-cobalt-manganternary ternary anode material is recycled
Technical field
The present invention relates to the method that nickel-cobalt-manganternary ternary anode material is recycled, belong to old and useless battery recovery technology field.
Background technology
Nickel-cobalt-manganternary ternary anode material system is developed by binary Ni-Mn sill, and calendar year 2001 OhZuku and Makimura has synthesized the trielement composite material LiNi of nNi:nCo:nMn=1:1:1 first 1/3co 1/3mn 1/3o 2, meanwhile Canadian Dahn etc. have studied the impact of change of component on positive pole material crystal structure, capacity, multiplying power discharging and thermal stability.Although LiNi 1/3co 1/3mn 1/3o 2search time is not long, but because of itself and LiCoO 2there is analog structure, possess good Research foundation, be namely considered to most possibly replace LiCoO once proposition 2, obtain national governments and support energetically.
Tertiary cathode material can be used for digital communication class battery, Notebook Battery, power tool battery, power bicycle/automobile batteries etc.In communication battery, in nearest 3-5 years, the leading position of cobalt acid lithium will weaken gradually, and may occur the phenomenon that cobalt acid lithium and nickel-cobalt-manganternary ternary anode material coexist, after 5 years, may be the epoch that nickel-cobalt-manganese ternary material is dominated exclusively.In field of power tools, nickel-cobalt-manganese ternary material has high energy density, good high rate during charging-discharging, outstanding cycle performance and security performance, likely becomes main positive electrode.
At present, the existing relevant report recycled about nickel-cobalt-manganternary ternary anode material.As: CN200810198972 to application discloses a kind of be the method that nickle cobalt lithium manganate prepared by raw material with waste and old lithium ion battery.Its main feature is: selecting cell positive material to be the waste and old lithium ion battery of nickle cobalt lithium manganate, lithium nickel cobalt dioxide etc. is raw material, through disassembling, sorting, pulverizing, after the preliminary treatment such as screening, adopt high temperature to remove binding agent, NaOH except after the techniques such as aluminium again, obtain nickeliferous, cobalt, manganese inactivation positive electrode; Then adopt that sulfuric acid and hydrogen peroxide system leach, P2O4 abstraction impurity removal, obtain pure nickel, cobalt, manganese solution, allocate suitable manganese sulfate, nickelous sulfate or cobaltous sulfate into, make nickel in solution, cobalt, manganese element mol ratio be 1:1:1; Adopt ammonium carbonate adjust ph subsequently, form nickel cobalt manganese carbonate precursor, then allocate appropriate lithium carbonate into, the activated nickle cobalt lithium manganate battery material of high temperature sintering synthesis tool.And for example: CN200710308154 discloses a kind of from containing the method reclaiming noble metal the battery slag of Co, Ni, Mn, it is for carrying out leaching to comprising the hydrochloric acid solution containing the roughly concentration of more than the lithium cell slag 250g/l of the lithium acid metal salt of Co, Ni and Mn of equivalent, or carry out heating leaching process with the sulfuric acid solution of the concentration of more than 200g/l, with acidic extractant, solvent extraction is carried out to leachate, extract roughly 100% of Mn and Co, generate the solution containing respective metal, from these solution, reclaim this metal.
Said method achieves the recycling of nickel-cobalt-manganternary ternary anode material, but by pulverizing, sieving separating nickel cobalt manganic acid lithium and aluminium foil, separating effect is bad; Adopt carbonate precipitation method to obtain nickel cobalt manganese carbonate precursor, easily cause the segregation of component in preparation process, the homogeneity of each Elemental redistribution of oxide can not be ensured, have impact on positive electrode chemical property; Organic solvent is adopted easily to cause secondary pollution.
Summary of the invention
Technical problem to be solved by this invention is to provide a kind of method that nickel-cobalt-manganternary ternary anode material is recycled.
The method that nickel-cobalt-manganternary ternary anode material of the present invention is recycled, comprise and remove binding agent step from the heat treatment of cobalt nickel lithium manganate ternary material positive plate, in its removal cobalt nickel lithium manganate ternary material positive plate, binding agent method is: by cobalt nickel lithium manganate ternary material positive plate in 400 ~ 1000 DEG C of heat treatment 0.5 ~ 5h.
Wherein, as preferred technical scheme, the method that nickel-cobalt-manganternary ternary anode material of the present invention is recycled comprises the steps:
A, waste lithium cell remaining capacity to be discharged, then disassemble battery, take out cobalt nickel lithium manganate ternary material positive plate;
B, by cobalt nickel lithium manganate ternary material positive plate in 400 ~ 1000 DEG C of vacuum baking 0.5 ~ 5h, then Ore Leaching is added, leaching process adds a small amount of nickel, cobalt, the manganese that reducing agent is used for being oxidized in reducing roasting process, obtains the mixed solution of nickel salt, cobalt salt, manganese salt, aluminium salt and lithium salts; Wherein, the consumption of reducing agent is that a small amount of nickel of oxidation, cobalt, manganese are reduced, and the reducing agent adopted is preferably at least one in sodium thiosulfate, hydrogen peroxide;
C, adjustment mixed solution pH value 3 ~ 9, preferably regulate mixed solution pH value to 3 ~ 7, make aluminum precipitation in solution, then filter and remove aluminium; Wherein, the conventional alkali lye such as NaOH, potassium hydroxide, lithium hydroxide can be adopted to regulate mixed solution pH value;
D, according to nickel cobalt Fe content in step c gained solution, add appropriate nickel cobalt mn sulphate and regulate nickel in solution, cobalt, manganese mol ratio to be 0.8 ~ 1.2:0.8 ~ 1.2:0.8 ~ 1.2;
E, add NaOH as precipitation reagent, add nickel, cobalt, manganese equal molar amount ammoniacal liquor as compounding ingredient, regulate solution ph to be 10 ~ 12, precipitation obtains nickel-cobalt-manganese ternary material precursor, filter, obtain lithium salt solution, lithium salt solution obtains lithium carbonate through purification precipitation;
F, nickel-cobalt-manganese ternary material precursor and lithium carbonate mixs by weight 2.4 ~ 2.6:1, then in 750 ~ 950 DEG C of calcining 12 ~ 24h, cool, obtain nickle cobalt lithium manganate.
Said method adopts acid+reducing agent system to leach, and NaOH is precipitation reagent synthesis nickle cobalt lithium manganate ternary anode material precursor, avoids generating Mn 3+or Mn (MnOOH) 4+(MnO 2), properties of product are reclaimed in impact, can not cause the segregation of component, ensure that the homogeneity of each Elemental redistribution of oxide, thus guarantee positive electrode stable electrochemical property in preparation process.
Further, the method that nickel-cobalt-manganternary ternary anode material of the present invention is recycled, in its b step, as fruit acid concentration is too high, then nickel, cobalt, manganese are oxidizable; As fruit acid concentration is too low, then the leaching rate of nickel, cobalt, manganese is on the low side, considers above-mentioned situation, preferably adopts that concentration is the sulfuric acid of 10 ~ 15wt%, hydrochloric acid or nitric acid leaches.
Further, in order to improve positive electrode chemical property, the method that above-mentioned nickel-cobalt-manganternary ternary anode material is recycled, in its Step d, preferably regulates the nickel in solution, cobalt, manganese mol ratio to be 1:1:1.
Wherein, the method that above-mentioned nickel-cobalt-manganternary ternary anode material is recycled, in order to make gained ternary material electrical property best, in its step e, when coprecipitated nickel hydroxide cobalt-manganese ternary material precursor, preferably also controlling reaction temperature is 40 ~ 90 DEG C.
The present invention has following beneficial effect: the inventive method achieves the recycling of nickle cobalt lithium manganate, eliminate the defect that existing recovery method exists, both be conducive to the sustainable development of industry on long terms, and indirectly reduced again the cost of nickel-cobalt-manganese ternary material, be conducive to popularizing of material.
Embodiment
The method that nickel-cobalt-manganternary ternary anode material of the present invention is recycled, comprise and remove binding agent step from the heat treatment of cobalt nickel lithium manganate ternary material positive plate, in its removal cobalt nickel lithium manganate ternary material positive plate, binding agent method is: by cobalt nickel lithium manganate ternary material positive plate in 400 ~ 1000 DEG C of heat treatment 0.5 ~ 5h.
Wherein, as preferred technical scheme, the method that nickel-cobalt-manganternary ternary anode material of the present invention is recycled comprises the steps:
A, waste lithium cell remaining capacity to be discharged, then disassemble battery, take out cobalt nickel lithium manganate ternary material positive plate;
B, by cobalt nickel lithium manganate ternary material positive plate in 400 ~ 1000 DEG C of vacuum baking 0.5 ~ 5h, then Ore Leaching is added, leaching process adds a small amount of nickel, cobalt, the manganese that reducing agent is used for being oxidized in reducing roasting process, obtains the mixed solution of nickel salt, cobalt salt, manganese salt, aluminium salt and lithium salts; Wherein, the consumption of reducing agent is that a small amount of nickel of oxidation, cobalt, manganese are reduced, and the reducing agent adopted is preferably at least one in sodium thiosulfate, hydrogen peroxide;
C, adjustment mixed solution pH value 3 ~ 9, preferably regulate mixed solution pH value to 3 ~ 7, make aluminum precipitation in solution, then filter and remove aluminium; Wherein, the conventional alkali lye such as NaOH, potassium hydroxide, lithium hydroxide can be adopted to regulate mixed solution pH value;
D, according to nickel cobalt Fe content in step c gained solution, add appropriate nickel cobalt mn sulphate and regulate nickel in solution, cobalt, manganese mol ratio to be 0.8 ~ 1.2:0.8 ~ 1.2:0.8 ~ 1.2;
E, add NaOH as precipitation reagent, add nickel, cobalt, manganese equal molar amount ammoniacal liquor as compounding ingredient, regulate solution ph to be 10 ~ 12, precipitation obtains nickel-cobalt-manganese ternary material precursor, filter, obtain lithium salt solution, lithium salt solution obtains lithium carbonate through purification precipitation;
F, nickel-cobalt-manganese ternary material precursor and lithium carbonate mixs by weight 2.4 ~ 2.6:1, then in 750 ~ 950 DEG C of calcining 12 ~ 24h, cool, obtain nickle cobalt lithium manganate.
Said method adopts acid+reducing agent system to leach, and NaOH is precipitation reagent synthesis nickle cobalt lithium manganate ternary anode material precursor, avoids generating Mn 3+or Mn (MnOOH) 4+(MnO 2), properties of product are reclaimed in impact, can not cause the segregation of component, ensure that the homogeneity of each Elemental redistribution of oxide, thus guarantee positive electrode stable electrochemical property in preparation process.
Further, the method that nickel-cobalt-manganternary ternary anode material of the present invention is recycled, in its b step, as fruit acid concentration is too high, then nickel, cobalt, manganese are oxidizable; As fruit acid concentration is too low, then the leaching rate of nickel, cobalt, manganese is on the low side, considers above-mentioned situation, preferably adopts that concentration is the sulfuric acid of 10 ~ 15wt%, hydrochloric acid or nitric acid leaches.
Further, in order to improve positive electrode chemical property, the method that above-mentioned nickel-cobalt-manganternary ternary anode material is recycled, in its Step d, preferably regulates the nickel in solution, cobalt, manganese mol ratio to be 1:1:1.
Wherein, the method that above-mentioned nickel-cobalt-manganternary ternary anode material is recycled, in order to make gained ternary material electrical property best, in its step e, when coprecipitated nickel hydroxide cobalt-manganese ternary material precursor, preferably also controlling reaction temperature is 40 ~ 90 DEG C.
Below in conjunction with embodiment, the specific embodiment of the present invention is further described, does not therefore limit the present invention among described scope of embodiments.
Embodiment 1 adopts the inventive method to recycle nickel-cobalt-manganternary ternary anode material
Discharged by waste nickel cobalt manganic acid lithium battery remaining capacity, disassemble battery, take out positive plate, battery case is pressed the classification such as aluminum hull, box hat, plastics and is reclaimed; By nickle cobalt lithium manganate positive plate through 1000 DEG C of calcining 0.5h.
Get the nickle cobalt lithium manganate positive plate 100kg after calcining, adopt the sulfuric acid leaching of 10wt%, leaching process adds sodium thiosulfate 1kg, obtains nickelous sulfate, cobaltous sulfate, manganese sulfate, aluminum sulfate and lithium sulfate mixed solution after leaching through filtering.Regulate mixed solution pH value 4.5, generate aluminum hydroxide precipitation, filter and remove aluminium hydroxide, obtain nickelous sulfate, cobaltous sulfate, manganese sulfate and lithium sulfate mixed solution.Add nickel cobalt mn sulphate in the solution and nickel cobalt manganese mol ratio is adjusted to 1:1:1, then NaOH is added as precipitation reagent, add proper ammonia as compounding ingredient, control reaction temperature 40 DEG C, pH value 12, precipitation obtains nickel-cobalt-manganese ternary material precursor, is separated by filtration, obtains lithium sulfate solution.
Nickel-cobalt-manganese ternary material precursor mixes with 34.7kg lithium carbonate ball milling, and mixture is placed in calciner, and in 750 DEG C of calcinings, constant temperature 12 hours, naturally cools in stove, obtain nickle cobalt lithium manganate tertiary cathode material.Lithium sulfate solution adds sodium carbonate precipitation and obtains lithium carbonate after concentrated.Reclaim obtained nickle cobalt lithium manganate tertiary cathode material chemical property as shown in table 1:
Table 1
Embodiment 2 adopts the inventive method to recycle nickel-cobalt-manganternary ternary anode material
Discharged by waste nickel cobalt manganic acid lithium battery remaining capacity, disassemble battery, take out positive plate, battery case is pressed the classification such as aluminum hull, box hat, plastics and is reclaimed; By nickle cobalt lithium manganate positive plate through 700 DEG C of roasting 3h.
Get the nickle cobalt lithium manganate positive plate 100kg after calcining, adopt the sulfuric acid leaching of 15wt%, leaching process adds sodium thiosulfate 0.8kg, obtains nickelous sulfate, cobaltous sulfate, manganese sulfate, aluminum sulfate and lithium sulfate mixed solution after leaching through filtering.Regulate mixed solution pH value 5, generate aluminum hydroxide precipitation, filter and remove aluminium hydroxide, obtain nickelous sulfate, cobaltous sulfate, manganese sulfate and lithium sulfate mixed solution.Add nickel cobalt mn sulphate in the solution and nickel cobalt manganese mol ratio is adjusted to 0.9:1:0.9, then NaOH is added as precipitation reagent, add proper ammonia as compounding ingredient, control reaction temperature 60 DEG C, pH value 10, precipitation obtains nickel-cobalt-manganese ternary material precursor, is separated by filtration, obtains lithium sulfate solution.
Nickel-cobalt-manganese ternary material precursor mixes with 34kg lithium carbonate ball milling, and mixture is placed in calciner, and in 950 DEG C of calcinings, constant temperature 24 hours, naturally cools in stove, obtain nickle cobalt lithium manganate tertiary cathode material.Lithium sulfate solution adds sodium carbonate precipitation and obtains lithium carbonate after concentrated.Reclaim obtained nickle cobalt lithium manganate tertiary cathode material chemical property as shown in table 2:
Table 2
Embodiment 3 adopts the inventive method to recycle nickel-cobalt-manganternary ternary anode material
Discharged by waste nickel cobalt manganic acid lithium battery remaining capacity, disassemble battery, take out positive plate, battery case is pressed the classification such as aluminum hull, box hat, plastics and is reclaimed; By nickle cobalt lithium manganate positive plate through 400 DEG C of roasting 5h.
Get the nickle cobalt lithium manganate positive plate 100kg after calcining, adopt the sulfuric acid leaching of 12wt%, leaching process adds sodium thiosulfate 1.2kg, obtains nickelous sulfate, cobaltous sulfate, manganese sulfate, aluminum sulfate and lithium sulfate mixed solution after leaching through filtering.Regulate mixed solution pH value 6, generate aluminum hydroxide precipitation, filter and remove aluminium hydroxide, obtain nickelous sulfate, cobaltous sulfate, manganese sulfate and lithium sulfate mixed solution.Add nickel cobalt mn sulphate in the solution and nickel cobalt manganese mol ratio is adjusted to 1:0.9:1, then NaOH is added as precipitation reagent, add proper ammonia as compounding ingredient, control reaction temperature 45 DEG C, pH value 11, precipitation obtains nickel-cobalt-manganese ternary material precursor, is separated by filtration, obtains lithium sulfate solution.
Nickel-cobalt-manganese ternary material precursor mixes with 35kg lithium carbonate ball milling, and mixture is placed in calciner, and in 850 DEG C of calcinings, constant temperature 15 hours, naturally cools in stove, obtain nickle cobalt lithium manganate tertiary cathode material.Lithium sulfate solution adds sodium carbonate precipitation and obtains lithium carbonate after concentrated.Reclaim obtained nickle cobalt lithium manganate tertiary cathode material chemical property as shown in table 3:
Table 3
Embodiment 4 adopts the inventive method to recycle nickel-cobalt-manganternary ternary anode material
Discharged by waste nickel cobalt manganic acid lithium battery remaining capacity, disassemble battery, take out positive plate, battery case is pressed the classification such as aluminum hull, box hat, plastics and is reclaimed; By nickle cobalt lithium manganate positive plate through 600 DEG C of roasting 4h.
Get the nickle cobalt lithium manganate positive plate 100kg after calcining, adopt the hydrochloric acid leaching of 12wt%, leaching process adds hydrogen peroxide 2.5kg, obtains nickel chloride, cobalt chloride, manganese chloride, aluminium chloride and lithium chloride mixed solution after leaching through filtering.Regulate mixed solution pH value 6, generate aluminum hydroxide precipitation, filter and remove aluminium hydroxide, obtain nickel chloride, cobalt chloride, manganese chloride and lithium chloride mixed solution.Add nickel cobalt-manganese salt in the solution and nickel cobalt manganese mol ratio is adjusted to 1:0.9:1, then add NaOH as precipitation reagent, add proper ammonia as compounding ingredient, control reaction temperature 45 DEG C, pH value 11, precipitation obtains nickel-cobalt-manganese ternary material precursor, be separated by filtration, obtain lithium chloride solution.
Nickel-cobalt-manganese ternary material precursor mixes with 35kg lithium carbonate ball milling, and mixture is placed in calciner, and in 850 DEG C of calcinings, constant temperature 15 hours, naturally cools in stove, obtain nickle cobalt lithium manganate tertiary cathode material.Lithium sulfate solution adds sodium carbonate precipitation and obtains lithium carbonate after concentrated.Reclaim obtained nickle cobalt lithium manganate tertiary cathode material chemical property as shown in table 3:
Table 3
Embodiment 5 adopts the inventive method to recycle nickel-cobalt-manganternary ternary anode material
Discharged by waste nickel cobalt manganic acid lithium battery remaining capacity, disassemble battery, take out positive plate, battery case is pressed the classification such as aluminum hull, box hat, plastics and is reclaimed; By nickle cobalt lithium manganate positive plate through 900 DEG C of roasting 1h.
Get the nickle cobalt lithium manganate positive plate 100kg after calcining, adopt the nitric acid leaching of 12wt%, leaching process adds hydrogen peroxide 2.5kg, obtains nickel nitrate, cobalt nitrate, manganese nitrate, aluminum nitrate and lithium nitrate mixed solution after leaching through filtering.Regulate mixed solution pH value 6, generate aluminum hydroxide precipitation, filter and remove aluminium hydroxide, obtain nickel nitrate, cobalt nitrate, manganese nitrate and lithium nitrate mixed solution.Add nickel cobalt-manganese salt in the solution and nickel cobalt manganese mol ratio is adjusted to 1:0.9:1, then add NaOH as precipitation reagent, add proper ammonia as compounding ingredient, control reaction temperature 45 DEG C, pH value 11, precipitation obtains nickel-cobalt-manganese ternary material precursor, be separated by filtration, obtain lithium nitrate solution.
Nickel-cobalt-manganese ternary material precursor mixes with 35kg lithium carbonate ball milling, and mixture is placed in calciner, and in 850 DEG C of calcinings, constant temperature 15 hours, naturally cools in stove, obtain nickle cobalt lithium manganate tertiary cathode material.Lithium sulfate solution adds sodium carbonate precipitation and obtains lithium carbonate after concentrated.Reclaim obtained nickle cobalt lithium manganate tertiary cathode material chemical property as shown in table 3:
Table 3
Embodiment 6 adopts the inventive method to recycle nickel-cobalt-manganternary ternary anode material
Discharged by waste nickel cobalt manganic acid lithium battery remaining capacity, disassemble battery, take out positive plate, battery case is pressed the classification such as aluminum hull, box hat, plastics and is reclaimed; By nickle cobalt lithium manganate positive plate through 800 DEG C of roasting 1.5h.
Get the nickle cobalt lithium manganate positive plate 100kg after calcining, adopt the sulfuric acid leaching of 12wt%, leaching process adds hydrogen peroxide 2.5kg, obtains nickelous sulfate, cobaltous sulfate, manganese sulfate, aluminum sulfate and lithium sulfate mixed solution after leaching through filtering.Regulate mixed solution pH value 6, generate aluminum hydroxide precipitation, filter and remove aluminium hydroxide, obtain nickelous sulfate, cobaltous sulfate, manganese sulfate and lithium sulfate mixed solution.Add nickel cobalt mn sulphate in the solution and nickel cobalt manganese mol ratio is adjusted to 1:0.9:1, then NaOH is added as precipitation reagent, add proper ammonia as compounding ingredient, control reaction temperature 45 DEG C, pH value 11, precipitation obtains nickel-cobalt-manganese ternary material precursor, is separated by filtration, obtains lithium sulfate solution.
Nickel-cobalt-manganese ternary material precursor mixes with 35kg lithium carbonate ball milling, and mixture is placed in calciner, and in 850 DEG C of calcinings, constant temperature 15 hours, naturally cools in stove, obtain nickle cobalt lithium manganate tertiary cathode material.Lithium sulfate solution adds sodium carbonate precipitation and obtains lithium carbonate after concentrated.Reclaim obtained nickle cobalt lithium manganate tertiary cathode material chemical property as shown in table 3:
Table 3

Claims (9)

1. the method for nickel-cobalt-manganternary ternary anode material recycling, is characterized in that comprising the steps:
A, waste lithium cell remaining capacity to be discharged, then disassemble battery, take out cobalt nickel lithium manganate ternary material positive plate;
B, by cobalt nickel lithium manganate ternary material positive plate in 400 ~ 1000 DEG C of vacuum baking 0.5 ~ 5h, then Ore Leaching is added, leaching process adds a small amount of nickel, cobalt, the manganese that reducing agent is used for being oxidized in reducing roasting process, obtains the mixed solution of nickel salt, cobalt salt, manganese salt, aluminium salt and lithium salts;
PH value to 3 ~ 9 of c, adjustment mixed solution, make aluminum precipitation in solution, then filter and remove aluminium;
D, according to nickel cobalt Fe content in mixed solution, add appropriate nickel cobalt-manganese salt and regulate nickel in solution, cobalt, manganese mol ratio to be 0.8 ~ 1.2:0.8 ~ 1.2:0.8 ~ 1.2;
E, add NaOH as precipitation reagent, add nickel, cobalt, manganese equal molar amount ammoniacal liquor as compounding ingredient, regulate solution ph to be 10 ~ 12, precipitation obtains nickel-cobalt-manganese ternary material precursor, filter, obtain lithium salt solution, lithium salt solution obtains lithium carbonate through purification precipitation;
F, nickel-cobalt-manganese ternary material precursor and lithium carbonate mixs by weight 2.4 ~ 2.6:1, then in 750 ~ 950 DEG C of calcining 12 ~ 24h, cool, obtain nickle cobalt lithium manganate.
2. the method recycled of nickel-cobalt-manganternary ternary anode material according to claim 1, is characterized in that in b step, adopts that concentration is the sulfuric acid of 10 ~ 15wt%, hydrochloric acid or nitric acid leaches; Described reducing agent is a kind of in sodium thiosulfate or hydrogen peroxide.
3. the method for nickel-cobalt-manganternary ternary anode material recycling according to claim 1 and 2, is characterized in that: in step c, regulates pH value to 3 ~ 7 of mixed solution.
4. the method for nickel-cobalt-manganternary ternary anode material recycling according to claim 1 and 2, is characterized in that: in Step d, regulates the nickel in solution, cobalt, manganese mol ratio to be 1:1:1.
5. the method for nickel-cobalt-manganternary ternary anode material recycling according to claim 3, is characterized in that: in Step d, regulates the nickel in solution, cobalt, manganese mol ratio to be 1:1:1.
6. the method for nickel-cobalt-manganternary ternary anode material recycling according to claim 1 and 2, is characterized in that: in step e, and when coprecipitated nickel hydroxide cobalt-manganese ternary material precursor, also controlling reaction temperature is 40 ~ 90 DEG C.
7. the method for nickel-cobalt-manganternary ternary anode material recycling according to claim 3, is characterized in that: in step e, and when coprecipitated nickel hydroxide cobalt-manganese ternary material precursor, also controlling reaction temperature is 40 ~ 90 DEG C.
8. the method for nickel-cobalt-manganternary ternary anode material recycling according to claim 4, is characterized in that: in step e, and when coprecipitated nickel hydroxide cobalt-manganese ternary material precursor, also controlling reaction temperature is 40 ~ 90 DEG C.
9. the method for nickel-cobalt-manganternary ternary anode material recycling according to claim 5, is characterized in that: in step e, and when coprecipitated nickel hydroxide cobalt-manganese ternary material precursor, also controlling reaction temperature is 40 ~ 90 DEG C.
CN201310104022.8A 2013-03-28 2013-03-28 Method for recycling nickel-cobalt-manganese ternary anode material Active CN103199320B (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
CN201310104022.8A CN103199320B (en) 2013-03-28 2013-03-28 Method for recycling nickel-cobalt-manganese ternary anode material
PCT/CN2014/074157 WO2014154152A1 (en) 2013-03-28 2014-03-27 Method for recycling nickel-cobalt-manganese ternary anode material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201310104022.8A CN103199320B (en) 2013-03-28 2013-03-28 Method for recycling nickel-cobalt-manganese ternary anode material

Publications (2)

Publication Number Publication Date
CN103199320A CN103199320A (en) 2013-07-10
CN103199320B true CN103199320B (en) 2015-05-27

Family

ID=48721742

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201310104022.8A Active CN103199320B (en) 2013-03-28 2013-03-28 Method for recycling nickel-cobalt-manganese ternary anode material

Country Status (2)

Country Link
CN (1) CN103199320B (en)
WO (1) WO2014154152A1 (en)

Families Citing this family (100)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103199320B (en) * 2013-03-28 2015-05-27 四川天齐锂业股份有限公司 Method for recycling nickel-cobalt-manganese ternary anode material
CN103606651A (en) * 2013-12-02 2014-02-26 河南师范大学 Method for preparing lithium nickelate cobaltate manganate cathode material by taking waste lithium ion batteries as raw material
CN104600284B (en) * 2015-01-15 2017-01-11 兰州理工大学 Method for regenerating positive active material in spent lithium manganate lithium ion battery
CN104659438B (en) * 2015-02-11 2017-03-01 江门市芳源环境科技开发有限公司 A kind of method that utilization refuse battery prepares ternary anode material precursor
CN104868190B (en) * 2015-05-13 2017-09-12 中国科学院过程工程研究所 The leaching of metal and recovery method in a kind of lithium ion cell anode waste
CN105375078B (en) * 2015-10-23 2017-12-12 李斌 A kind of method that spherical nickel-cobalt mangaic acid lithium is prepared by based lithium-ion battery positive plate circulation
CN105633500A (en) * 2016-02-22 2016-06-01 四川天齐锂业股份有限公司 Method for preparing ternary cathode material precursor by recycling lithium-ion battery material
CN105789726A (en) * 2016-04-21 2016-07-20 苏州聚智同创环保科技有限公司 Method for preparing nickel-cobalt-manganese ternary material precursor from waste lithium ion battery
CN106299526B (en) * 2016-09-19 2018-11-06 中国电子科技集团公司第十八研究所 Recycling method of strong alkali solution in waste lithium battery recycling industry
CN106450552A (en) * 2016-10-26 2017-02-22 荆门市格林美新材料有限公司 Method for preparing ternary cathode material from waste lithium cobalt oxide cathode material
CN106450548A (en) * 2016-10-26 2017-02-22 荆门市格林美新材料有限公司 Method for preparing ternary cathode materials by waste lithium manganate cathode materials
CN106328927A (en) * 2016-11-03 2017-01-11 王坚 Resource recycling method of waste battery cathode materials
CN106785167B (en) * 2016-12-20 2018-12-28 天齐锂业股份有限公司 The recovery method of lithium in waste lithium cell positive electrode
CN106784793A (en) * 2016-12-31 2017-05-31 深圳市沃特玛电池有限公司 The preparation method of ternary cathode material of lithium ion battery
TWI746818B (en) * 2017-04-07 2021-11-21 比利時商烏明克公司 Process for the recovery of lithium
CN107196004B (en) * 2017-05-13 2019-07-19 合肥国轩高科动力能源有限公司 Method for recovering valuable metals from waste lithium ion power batteries
CN107117661B (en) * 2017-05-26 2019-01-25 金川集团股份有限公司 The method for preparing ternary hydroxide using nickel cobalt manganese in the waste and old lithium ion battery of liquid phase method recycling
CN107275704A (en) * 2017-06-13 2017-10-20 安化县泰森循环科技有限公司 A kind of recovery method of ternary battery anode slice
CN107419096B (en) * 2017-06-27 2019-07-16 安徽巡鹰新能源科技有限公司 A kind of preparation method of waste lithium cell reclaiming tertiary cathode material
CN107394199A (en) * 2017-07-20 2017-11-24 北京理工大学 The restoration methods of chemical property after a kind of nickelic tertiary cathode material storage
CN107768763B (en) * 2017-10-19 2019-06-21 陈明海 A kind of method of waste and old lithium ion battery recycling production NCM salt
CN109921014B (en) * 2017-12-13 2021-10-01 荆门市格林美新材料有限公司 Nickel-based lithium ion battery anode material with sub-crystal structure and preparation method thereof
CN108103323B (en) * 2017-12-14 2019-10-22 中南大学 A kind of recovery method of the positive electrode of nickel cobalt manganese old and useless battery
CN107986335A (en) * 2017-12-14 2018-05-04 上海第二工业大学 A kind of method that manganese dioxide particle is prepared using waste and old ternary dynamic lithium battery positive electrode
CN107946688A (en) * 2017-12-16 2018-04-20 淄博国利新电源科技有限公司 The method that lithium is recycled from discarded ternary lithium ion battery
CN108172925A (en) * 2017-12-27 2018-06-15 浙江中金格派锂电产业股份有限公司 A kind of nickle cobalt lithium manganate ter-polymers cell anode waste recovery method
CN108400401A (en) * 2018-02-27 2018-08-14 四川省有色冶金研究院有限公司 A method of using the active material of waste and old lithium dynamical battery separation as Material synthesis nickle cobalt lithium manganate
CN110277552B (en) * 2018-03-16 2022-07-15 荆门市格林美新材料有限公司 Method for repairing and regenerating nickel-cobalt-manganese ternary cathode material in waste battery
CN108598396A (en) * 2018-03-30 2018-09-28 华南师范大学 A kind of preparation method of regenerative lithium ion anode material
CN108649291A (en) * 2018-05-24 2018-10-12 北京化工大学 It is a kind of using waste and old lithium ion battery as the technique of raw materials recovery nickel-cobalt lithium manganate cathode material
CN108682915A (en) * 2018-05-29 2018-10-19 江苏理工学院 A kind of waste and old nickel-cobalt-manganese ternary lithium battery and silver-nickel are jointly processed by method
CN108879008A (en) * 2018-06-21 2018-11-23 南充中芯新能源科技有限公司 A kind of recovery and treatment method and nickle cobalt lithium manganate battery material of waste lithium cell positive electrode
CN108878836B (en) * 2018-06-28 2020-12-22 山东理工大学 Method for directly preparing lithium zincate modified ternary cathode material by using waste lithium battery cathode material
CN108899604B (en) * 2018-06-28 2020-10-27 郑州中科新兴产业技术研究院 Method for preparing ternary positive electrode material precursor by utilizing waste lithium battery positive electrode piece
CN108933308B (en) * 2018-07-13 2020-05-05 江西环锂新能源科技有限公司 Comprehensive recycling method for anode and cathode of scrapped lithium battery
CN109256596B (en) * 2018-09-19 2020-09-04 中国科学院青海盐湖研究所 Method and system for reversely preparing aluminum-doped ternary precursor
CN109234524B (en) * 2018-09-19 2020-04-14 中国科学院青海盐湖研究所 Method and system for comprehensively recovering valuable metals from waste ternary lithium batteries
CN109449434B (en) * 2018-09-20 2021-08-20 广东佳纳能源科技有限公司 Method for preparing ternary lithium battery positive electrode material precursor by using waste lithium ion battery
EP3874071A1 (en) * 2018-10-30 2021-09-08 Albemarle Corporation Processes for extracting metals from lithium-ion batteries
CN109256599A (en) * 2018-11-07 2019-01-22 深圳佳彬科技有限公司 A kind of processing method for nickel-cobalt-manganese ternary waste lithium cell
CN109735709B (en) * 2018-12-13 2021-01-08 江西赣锋循环科技有限公司 Method for recycling lithium from calcium and magnesium removing slag and preparing ternary precursor material
JP7175756B2 (en) * 2018-12-27 2022-11-21 Jx金属株式会社 Valuable metal recovery method
CN109755539A (en) * 2019-02-21 2019-05-14 湖南邦普循环科技有限公司 Utilize the method for lithium ion cell anode waste production aluminium doping ternary precursor
CN109904548A (en) * 2019-03-22 2019-06-18 郑州中科新兴产业技术研究院 A method of synthesizing rich lithium material from waste and old lithium ion battery
CN110040786A (en) * 2019-04-18 2019-07-23 甘肃睿思科新材料有限公司 A kind of method of anode material of lithium battery recycling and reusing
CN110034350B (en) * 2019-04-23 2022-07-12 南昌大学 Method for comprehensively recycling waste lithium batteries through low-oxygen cracking
CN110157915A (en) * 2019-06-24 2019-08-23 甘肃睿思科新材料有限公司 The efficient reuse method of anode material of lithium battery
CN110233306A (en) * 2019-07-09 2019-09-13 郑州中科新兴产业技术研究院 A kind of method of waste and old lithium ion battery recycling ternary anode material precursor
CN110498434B (en) * 2019-07-26 2021-08-20 广东佳纳能源科技有限公司 Recovery method and application of lithium ion battery positive electrode active material
CN110422891A (en) * 2019-08-08 2019-11-08 中国科学院青海盐湖研究所 A kind of method preparing nickel-cobalt-manganese ternary presoma, system and application
CN110980817B (en) * 2019-10-10 2022-06-14 格林美(无锡)能源材料有限公司 High-power and long-cycle lithium battery positive electrode material and preparation method thereof
CN111115662B (en) * 2019-12-31 2021-03-09 清华四川能源互联网研究院 Lithium battery material recovery method
CN111403842B (en) * 2020-04-03 2022-02-18 万华化学集团股份有限公司 Recovery method of waste lithium battery anode material, spherical nickel oxide material and application
CN111458379A (en) * 2020-04-08 2020-07-28 宁波容百新能源科技股份有限公司 Method for judging mixing degree of ternary precursor reaction kettle of lithium ion battery
CN111477985B (en) * 2020-04-15 2023-08-15 中南大学 Method for recycling waste lithium ion batteries
CA3173753A1 (en) * 2020-04-23 2021-10-28 Jx Nippon Mining & Metals Corporation Method for producing mixed metal salt
CN111786008B (en) * 2020-07-10 2022-04-05 中国矿业大学 Multi-process efficient and synergistic recycling method for retired lithium ion battery positive electrode material
CN111807423A (en) * 2020-07-22 2020-10-23 成都理工大学 Method for preparing battery anode material by leaching waste lithium battery with sulfur dioxide gas
CN111987381A (en) * 2020-08-25 2020-11-24 长沙矿冶研究院有限责任公司 Method for synchronously defluorinating valuable metals leached from waste lithium ion batteries
CN111960480A (en) * 2020-08-28 2020-11-20 四川省有色冶金研究院有限公司 Method for preparing nickel-cobalt-manganese ternary material by using waste lithium ion battery
CN114180646B (en) * 2020-09-15 2024-01-26 中国石油化工股份有限公司 Positive electrode material precursor, preparation method thereof, positive electrode material and application thereof
CN112725621B (en) * 2020-09-17 2022-10-14 湖北金泉新材料有限公司 Method for separating nickel, cobalt and manganese from waste lithium battery based on carbonate solid-phase conversion method
CN112374548A (en) * 2020-09-30 2021-02-19 宜宾光原锂电材料有限公司 Method for treating high-iron material containing nickel-cobalt-manganese hydroxide
CN112374511B (en) * 2020-10-17 2022-02-11 北京科技大学 Method for preparing lithium carbonate and ternary precursor by recycling waste ternary lithium battery
CN112239232A (en) * 2020-10-20 2021-01-19 西安富阎时代新能源有限公司 Process for recycling waste ternary lithium ion battery anode material
CN112442597A (en) * 2020-10-21 2021-03-05 荆门市格林美新材料有限公司 Method for comprehensively treating materials in nickel-cobalt-manganese ternary precursor washing wastewater
CN112786988B (en) * 2020-11-26 2022-06-14 清华四川能源互联网研究院 Impurity removal and treatment method in recovery process of scrapped positive electrode material of lithium battery
CN112813270B (en) * 2020-12-30 2024-07-02 江苏海普功能材料有限公司 Method for recycling waste nickel-cobalt-manganese ternary lithium battery anode material
CN112830526B (en) * 2021-01-04 2023-10-13 赣州有色冶金研究所有限公司 Method for regenerating ternary precursor by using nickel-cobalt-manganese slag
CN112875767B (en) * 2021-01-28 2023-01-17 山东宏匀纳米科技有限公司 Method for preparing ternary cathode material by using lignin as fuel through solution combustion method
CN113151680B (en) * 2021-02-08 2023-06-16 中国科学院宁波材料技术与工程研究所 Method for recycling waste lithium batteries
CN113086996A (en) * 2021-03-25 2021-07-09 宁夏百川新材料有限公司 Recycling method of waste ternary fluorine-doped battery positive electrode material
CN113186410A (en) * 2021-04-27 2021-07-30 中国恩菲工程技术有限公司 Method for recovering valuable metal lithium from waste lithium ion battery anode material
CN115611321A (en) * 2021-05-31 2023-01-17 福建师范大学 Method for preparing sodium ion battery positive electrode material by recycling waste battery positive electrode (nickel cobalt lithium manganate) and application
CN113998742A (en) * 2021-09-27 2022-02-01 中天新兴材料有限公司 Recycling method of nickel-cobalt-manganese ternary lithium battery
CN114069083B (en) * 2021-10-12 2024-07-09 广东邦普循环科技有限公司 Method for recycling and synthesizing high-safety anode material from anode scraps and application of high-safety anode material
CN113943020A (en) * 2021-10-15 2022-01-18 广东瑞科美电源技术有限公司 Regenerated lithium cobaltate and activation method and application thereof
CN113943021A (en) * 2021-10-15 2022-01-18 广东瑞科美电源技术有限公司 Regenerated lithium cobaltate and repairing method and application thereof
CN114085995A (en) * 2021-11-09 2022-02-25 湖北亿纬动力有限公司 Method for preparing metal simple substance and compound thereof by recycling waste lithium ion battery and application thereof
CN114196829B (en) * 2021-11-17 2023-03-28 华中科技大学 Method for recovering nickel-cobalt-manganese cathode material of retired lithium ion battery
CN116199263A (en) * 2021-12-01 2023-06-02 中国科学院福建物质结构研究所 Method for preparing functional adsorption material beta-MnO 2 from waste battery
CN113921932B (en) * 2021-12-14 2022-04-01 矿冶科技集团有限公司 Precursor solution, preparation method thereof, positive electrode material and lithium ion battery
CN114314617B (en) * 2021-12-23 2023-06-30 北京化工大学 Method for recycling metal from waste ternary lithium ion battery anode material
CN114291854A (en) * 2021-12-30 2022-04-08 中南大学 Treatment method for recycling waste battery anode material
CN115810742A (en) * 2022-01-05 2023-03-17 宁德时代新能源科技股份有限公司 Preparation method of positive electrode active material
CN114477314A (en) * 2022-01-28 2022-05-13 齐鲁工业大学 Preparation method and application of nickel-cobalt-manganese ternary cathode material
CN114684872B (en) * 2022-03-09 2023-08-11 江门市长优实业有限公司 Carbon reduction roasting recovery method for ternary positive electrode waste
CN114644366A (en) * 2022-03-16 2022-06-21 贵州大学 Lithium cobaltate closed-loop recovery method of waste lithium ion battery based on eutectic solvent
CN114597534A (en) * 2022-03-29 2022-06-07 西安交通大学 Method for in-situ repairing of waste ternary lithium battery cathode material through supercritical water
CN115725866B (en) * 2022-11-21 2023-12-22 北京工业大学 Method for preferentially recycling manganese from waste lithium-rich manganese-based positive electrode material
CN115784324B (en) * 2022-11-29 2024-04-12 四川蜀矿环锂科技有限公司 Method for recycling and preparing ternary positive electrode material precursor by using waste ternary lithium battery
CN115739108B (en) * 2022-12-05 2023-06-06 广东省科学院生态环境与土壤研究所 Resource utilization method of waste lithium ion battery
CN115849462B (en) * 2022-12-07 2024-04-09 合肥国轩高科动力能源有限公司 Nickel-cobalt-manganese ternary positive electrode material and preparation method and application thereof
CN116177620A (en) * 2023-01-17 2023-05-30 四川蜀矿环锂科技有限公司 Method for regenerating and synthesizing positive electrode material precursor by using waste ternary lithium battery
CN115961141A (en) * 2023-02-01 2023-04-14 中国地质科学院郑州矿产综合利用研究所 Eutectic solvent and preparation method and application thereof
CN115852152B (en) * 2023-02-28 2023-05-16 矿冶科技集团有限公司 Method for cooperatively treating battery black powder and nickel cobalt hydroxide
CN116354402B (en) * 2023-03-02 2024-08-09 福州大学 Treatment method of waste lithium manganate ion battery anode material
CN116495791A (en) * 2023-03-31 2023-07-28 南通金通储能动力新材料有限公司 Method for efficiently utilizing ternary precursor wastewater
CN116947113A (en) * 2023-07-31 2023-10-27 甘肃睿思科新材料有限公司 Treatment method of lithium cobaltate and lithium manganate mixed waste
CN118248979A (en) * 2024-04-12 2024-06-25 江苏天能新材料有限公司 Method for separating positive electrode material from waste lithium ion battery

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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
CN101969148A (en) * 2010-10-15 2011-02-09 中南大学 Pretreatment method for recovering valuable metal from anode material of waste lithium ion battery

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1324758C (en) * 2005-04-25 2007-07-04 武汉理工大学 Method for separating and recovering cobalt from waste lithium ion cell
CN101376510B (en) * 2008-09-25 2010-07-14 中南大学 Method for preparing nano-scale magnesium hydrate by extracting magnesium from low grade laterite nickel ore hydrochloric acid leaching liquid
CN101450815A (en) * 2008-10-07 2009-06-10 佛山市邦普镍钴技术有限公司 Method for preparing nickel and cobalt doped lithium manganate by using waste and old lithium ionic cell as raw material
CN103199320B (en) * 2013-03-28 2015-05-27 四川天齐锂业股份有限公司 Method for recycling nickel-cobalt-manganese ternary anode material

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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
CN101969148A (en) * 2010-10-15 2011-02-09 中南大学 Pretreatment method for recovering valuable metal from anode material of waste lithium ion battery

Also Published As

Publication number Publication date
CN103199320A (en) 2013-07-10
WO2014154152A1 (en) 2014-10-02

Similar Documents

Publication Publication Date Title
CN103199320B (en) Method for recycling nickel-cobalt-manganese ternary anode material
CN108878866B (en) Method for preparing ternary material precursor and recovering lithium by using ternary cathode material of waste lithium ion battery
CN111129632B (en) Method for recycling anode and cathode mixed materials of waste ternary lithium ion battery
CN105958148B (en) A method of recycling valuable metal from waste and old nickle cobalt lithium manganate battery material
Yang et al. Short process for regenerating Mn-rich cathode material with high voltage from mixed-type spent cathode materials via a facile approach
CN111206148A (en) Method for recycling and preparing ternary cathode material by using waste ternary lithium battery
CN111477985B (en) Method for recycling waste lithium ion batteries
Gao et al. Recycling LiNi0. 5Co0. 2Mn0. 3O2 material from spent lithium-ion batteries by oxalate co-precipitation
CN108649291A (en) It is a kind of using waste and old lithium ion battery as the technique of raw materials recovery nickel-cobalt lithium manganate cathode material
CN111254294B (en) Method for selectively extracting lithium from waste lithium ion battery powder and recovering manganese dioxide through electrolytic separation
CN109755539A (en) Utilize the method for lithium ion cell anode waste production aluminium doping ternary precursor
CN102030375A (en) Method for preparing lithium cobaltate by directly using failed lithium ion battery
CN101450815A (en) Method for preparing nickel and cobalt doped lithium manganate by using waste and old lithium ionic cell as raw material
CN101831548A (en) Method for recovering valuable metals from waste lithium manganese oxide battery
CN101555030A (en) Method for recovering and recycling waste lithium ion battery cathode material
CN105098281B (en) The method that polynary positive pole material is reclaimed from waste and old polynary power lithium-ion battery
CN110092398B (en) Resource utilization method for waste lithium ion battery roasting tail gas
CN104466294B (en) The method reclaiming metal from waste LiCoxNiyMnzO 2 battery
CN104538696A (en) Method for recycling metal from waste lithium ion battery with Ni-Co lithium manganite positive electrode materials
CN104466295A (en) Method for regenerating positive electrode active material in LiNi1/3Co1/3Mn1/3O2 waste lithium ion battery
Shen et al. Recycling cathodes from spent lithium-ion batteries based on the selective extraction of lithium
CN113200574A (en) Method for regenerating lithium-rich manganese-based positive electrode from mixed waste lithium battery
CN104538695A (en) Method for recycling metal in waste LiMn1-x-yNixCoyO2 battery and preparing LiMn1-x-yNixCoyO2
WO2014154154A1 (en) Method of recycling lithium manganese battery anode material
EP3951979B1 (en) Method for separating transition metal from waste cathode material

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C56 Change in the name or address of the patentee
CP03 Change of name, title or address

Address after: 629200 Shehong County, Suining City, Taihe Town, north of the city of Qi Qi lithium Limited by Share Ltd

Patentee after: Tianqi Lithium Co., Ltd.

Address before: 629200, Sichuan County, Suining City, Shehong Province Taihe Town North Village space, Sichuan Tianqi lithium industry Limited by Share Ltd

Patentee before: Sichuan Tianqi Lithium Industries.Inc.

TR01 Transfer of patent right

Effective date of registration: 20191016

Address after: 629200, Suining County, Sichuan City, Shehong Province Taihe Town, North Qi Li lithium Limited by Share Ltd

Co-patentee after: Tianqi lithium industry (Jiangsu) Co., Ltd.

Patentee after: Tianqi Lithium Industry Co., Ltd.

Co-patentee after: Tianqi Lithium Industry (Shehong) Co., Ltd.

Address before: 629200, Suining County, Sichuan City, Shehong Province Taihe Town, North Qi Li lithium Limited by Share Ltd

Patentee before: Tianqi Lithium Industry Co., Ltd.

TR01 Transfer of patent right
CP03 Change of name, title or address

Address after: 215634, 5, Dongxin Road, Yangzi International Chemical Industry Park, Suzhou, Jiangsu, Zhangjiagang

Co-patentee after: Tianqi Lithium Industry Co., Ltd.

Patentee after: Tianqi lithium industry (Jiangsu) Co., Ltd.

Co-patentee after: Tianqi Lithium Industry (Shehong) Co., Ltd.

Address before: 629200, Suining County, Sichuan City, Shehong Province Taihe Town, North Qi Li lithium Limited by Share Ltd

Co-patentee before: Tianqi lithium industry (Jiangsu) Co., Ltd.

Patentee before: Tianqi Lithium Industry Co., Ltd.

Co-patentee before: Tianqi Lithium Industry (Shehong) Co., Ltd.

CP03 Change of name, title or address