CN105810894A - Multilayer coated structure lithium ion battery positive electrode material preparation method - Google Patents

Multilayer coated structure lithium ion battery positive electrode material preparation method Download PDF

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CN105810894A
CN105810894A CN201410848430.9A CN201410848430A CN105810894A CN 105810894 A CN105810894 A CN 105810894A CN 201410848430 A CN201410848430 A CN 201410848430A CN 105810894 A CN105810894 A CN 105810894A
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solution
lithium
preparation
ion batteries
ammonium
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宋顺林
刘亚飞
陈彦彬
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Beijing Easpring Material Technology Co Ltd
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Beijing Easpring Material Technology Co Ltd
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    • 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Abstract

The invention discloses a multilayer coated structure lithium ion battery positive electrode material preparation method. The preparation method comprises preparing a spherical core through a reaction through a liquid phase sedimentation method, adding reaction solutions with different formulas into the spherical core in a concurrent flow way so that precipitates grow on the spherical surface of the inner core, carrying out one or more layer coating through a spheroidization preparation device and method to obtain a multilayer-coated spherical precursor material and carrying out mixing sintering on the precursor material and a lithium salt to obtain the lithium ion battery positive electrode material. The preparation method simplifies equipment and operation processes, reduces a cost, has a smooth process, can easily control reaction system and product index stability and obviously improves product performances.

Description

A kind of preparation method of the anode material for lithium-ion batteries of multilayer coating structure
Technical field
The preparation method that the present invention relates to the anode material for lithium-ion batteries of a kind of multilayer coating structure, in particular relates to the continuous preparation method of the spherical multicomponent material of a kind of lithium ion battery multilayer coating structure.
Background technology
Lithium ion battery multicomponent material is generally LiNixCoyMn1-x-yMO2Form, in its solid solution, the raising specific capacity along with Ni content increases to some extent, such as LiNi0.8Co0.1Mn0.1O2Reversible capacity is up to 190mAh/g, considerably beyond LiCoO2(the lithium electricity positive electrode that application is maximum at present, specific capacity is about 145mAh/g), but the cycle performance of material, security performance decline therewith, how when not sacrificing capacity, simultaneously improve its circulation and security performance, become problem demanding prompt solution.
Multicomponent material presoma is generally spherical morphology, its performance directly influences multicomponent material and the performance of lithium ion battery made thereof, patent document CN101997113A provides a kind of technology in the process prepare presoma, material being coated with, to solve the performance issue of above-mentioned multicomponent material, its kernel adopts nickelic formula, prepares lithium ion battery and can play the height ratio capacity advantage of material;Clad adopts low nickel or without nickel formula, it is possible to increase the high temperature cyclic performance of battery and security performance.Adopting the capacity of lithium ion battery that this material is prepared high, battery tympanites is little, and high temperature circulation is stable, safety is high, and material preparation process is simple, relative inexpensiveness.
Sphere material generally can adopt the liquid phase deposition of interval to prepare, and is namely initially formed kernel precipitation and is collected, is subsequently adding in synthesis reactor as end liquid again at Surface Creation clad, and the reaction of interruption prepares the sphere material of multilayer coating structure.Patent document CN1635649 adopts batch process to be coated with one layer of cobalt hydroxide at ball shape nickel hydroxide surface, but batch process there is also the defect of self, preparation process and product index less stable, and technological process is smooth and easy not, and more difficult in control, processing cost is higher.Patent document CN1206072 discloses the continuous preparation method of a kind of spherical powder, at a certain temperature, respectively certain density nickel salt, sodium hydroxide, ammonia or the form with nickel salt+ammonia, sodium hydroxide+ammonia are continuously added in reactor, controlling the pH value of reaction system, reactant mean residence time and stirring condition, nickel hydroxide crystallizes out with spheroidal particle.Achieve the control of nickel hydroxide mean diameter and particle size distribution in this patent, but the method only achieves the preparation of ball material, prepared by the continuous way of unrealized multilayer coating structure sphere material.
Summary of the invention
The preparation method of the anode material for lithium-ion batteries of a kind of multilayer coating structure provided by the invention, this process simplify equipment and operation sequence, reduce cost, technological process ratio is smoothly, the stability of reaction system and product index can be controlled with comparalive ease, and properties of product obtain and are obviously improved.
Technical scheme is as follows:
The preparation method of the anode material for lithium-ion batteries of a kind of multilayer coating structure, comprises the steps:
(1) with liquid phase deposition, nucleation reaction solution is continued and in the nucleation reactor (0) that is injected into of stream, control reaction solution concentration 1 ~ 2mol/L, response time 5 ~ 30h, make reacted serosity naturally overflow in first order reaction still (1);
(2) being continued by coating solution and stream is injected in first order reaction still (1), control the concentration 1 ~ 2mol/L of coating solution, response time 1 ~ 30h, reacted serosity overflows in secondary response still (2) naturally;
(3) serosity after ageing, by material filtering, washing, dries, obtains the spherical precursor material of spherical one layer cladding in secondary response still (2);
When being coated with number of plies n > 1,
(4) n order reaction still serosity is constantly to n+1 order reaction still overflow, is continued by coating solution and stream is injected in n+1 order reaction still, controls response time 1 ~ 30h, and reacted serosity overflows in n+2 order reaction still naturally;Serosity after ageing, by material filtering, washing, dries, obtains the spherical precursor material of spherical n layer clad structure in n+2 order reaction still;
(5) by above-mentioned persursor material and lithium salts mix, under air or oxygen atmosphere, sintering prepares the anode material for lithium-ion batteries of multilayer coating structure.
In above-mentioned preparation method, the described cladding number of plies is generally 1-5.
Preferably, in above-mentioned preparation method, the reactor in each step is both preferably stirred autoclave.
In above-mentioned preparation method, in described step (1), nucleation reaction solution all includes metal mixed saline solution with coating solution in step (2), (4), and its metal consists of NixM1-x, wherein 0.5≤x≤1.0 in step (1), 0≤x≤0.5 in step (2), (4), one or more in Co, Mn, Fe, Mg, Ca, Sr, Ba, B, Al, Y, Sm, Ti, Zn, Zr, Nb, Mo or W of M.
In above-mentioned preparation method, the salt a kind of or wherein several mixture in sulfate, chlorate, nitrate, acetate or alkoxide in described metal mixed saline solution.
In above-mentioned preparation method, in described step (1), nucleation reaction solution all includes precipitant with coating solution in step (2), (4), the precipitant a kind of or wherein several mixture in ammonia, sodium hydroxide, potassium hydroxide, Lithium hydrate, sodium dihydrogen phosphate, disodium hydrogen phosphate, potassium dihydrogen phosphate, dipotassium hydrogen phosphate, ammonium phosphate, ammonium hydrogen carbonate, ammonium carbonate, sodium bicarbonate, sodium carbonate, potassium carbonate, sodium fluoride, ammonium fluoride.
In above-mentioned preparation method, in described step (1), in nucleation reaction solution and step (2), (4), coating solution can also include reaction promoter, and reaction promoter is selected from a kind of in EDTA, ammonia, ammonium chloride, ammonium sulfate, ammonium nitrate, air, oxygen, ozone, hydrogen peroxide, sodium hypochlorite, sodium peroxydisulfate, nitrogen or wherein several nonreactive mixture.
In above-mentioned preparation method, the scope of the final anode material for lithium-ion batteries meso-position radius prepared is 3 ~ 25 μm.
Principles of the invention is: adopt liquid phase deposition, successive reaction prepares spherical inner core, simultaneously by the reaction solution of different formulations and flow addition, it is deposited in the spherical surface cladding growth of kernel, one layer of clad structure persursor material to multilamellar is realized by continuous way preparation facilities and method, again persursor material is mixed with lithium source, sinters, finally give the anode material for lithium-ion batteries of multilayer coating structure.
The present invention has an advantage that
1. adopt continuity method to prepare the ball-shaped lithium-ion battery anode material of multilayer coating structure, devise a set of reaction method and device, decrease unnecessary centrifugation apparatus compared with batch process, simplify operation sequence, reduce cost.
2. by reacting pH, temperature, the control of time, it is possible to realize continuously performing of reaction;Technological process ratio is smoothly, it is possible to be relatively easy to control the stability of reaction system and product index.
3. compared with batch process, more prominent, the anode material for lithium-ion batteries of multilayer coating structure prepared by employing continuity method, production efficiency is higher, and quality consistency is higher, and product is finer and close, and pattern and covered effect are better.
Embodiment 1
nullBy nickel sulfate、Cobaltous sulfate,The mixing salt solution (1) obtaining 2mol/L is dissolved according to the metal molar ratio than 0.80:0.20,By mixing salt solution (1)、10.5mol/L ammonia spirit,The sodium hydroxide solution of 10mol/L and flows in the nucleation reactor adding stirring simultaneously,The control response time is 30h,The pH value of reaction system solution is 12.3,It is 60 DEG C that heating in water bath controls temperature,Reacted serosity is made naturally to overflow in first order reaction still,By Nickel dichloride.、Cobaltous chloride、Manganese chloride、Magnesium chloride dissolves the mixing salt solution (2) obtaining 2mol/L according to the metal molar ratio than 0.33:0.33:0.33:0.01,By mixing salt solution (2)、10.5mol/L ammonia、The sodium hydroxide solution of 10mol/L and flows in the first order reaction still adding stirring simultaneously,Reaction is at N2Carrying out under atmosphere protection, the control response time is 29h, and the pH value of reaction system solution is 11.0, and it is 60 DEG C that heating in water bath controls temperature, in core surface cladding growth, by material filtering, washing, drying after reaction, obtains the spherical precursor material of one layer of cladding.By above-mentioned persursor material and Lithium hydrate mix, in air atmosphere, 880 DEG C of sintering 15h, prepare the anode material for lithium-ion batteries of one layer of clad structure, testing this positive electrode meso-position radius is 15.3mm.
Embodiment 2
1.5mol/L nickel nitrate solution, the sodium hydroxide solution of 8mol/L, 5mol/L ammonia simultaneously and are flowed in the nucleation reactor adding stirring, the control response time is 30h, the pH value of reaction system solution is 12.6, and controlling temperature is 55 DEG C, and precipitation nature overflows in first order reaction still.
Nickel nitrate, manganese nitrate are dissolved the mixing salt solution (2) obtaining 1.8mol/L according to the metal molar ratio than 0.5:0.5, by mixing salt solution (2), the ammonium sulfate of 2mol/L, 5mol/L potassium hydroxide solution simultaneously and flow in the first order reaction still adding stirring, reaction is at N2Carrying out under atmosphere protection, the control response time is 20h, and the pH value of reaction system solution is 11.0, and it is 55 DEG C that heating in water bath controls temperature, and reacted one layer of serosity overflows in secondary response still naturally.
Cobaltous acetate, manganese acetate are dissolved the mixing salt solution (3) obtaining 1.5mol/L according to the metal molar ratio than 0.5:0.5, the disodium phosphate soln of mixing salt solution (3), 2mol/L simultaneously and is flowed in the secondary response still adding stirring, the control response time is 19h, the pH value of reaction system solution is 9.2, it is 55 DEG C that heating in water bath controls temperature, reacted two layers of cladding serosity, through precipitation, washing, dry, obtain the spherical precursor material of two layers of clad structure.By above-mentioned persursor material and lithium carbonate mix, in air atmosphere, 920 DEG C of sintering 12h, prepare the anode material for lithium-ion batteries of two layers of clad structure, testing this positive electrode meso-position radius is 23.1mm.
Embodiment 3
Nickel acetate, cobaltous acetate, manganese acetate are dissolved according to the metal molar ratio than 0.60:0.20:0.20 and obtains the mixing salt solution of 2.0mol/L, the sodium carbonate liquor of 2mol/L, 2mol/L ammonium carbonate and simultaneously and flow in the nucleation reactor adding stirring, the control response time is 5h, the pH value of the solution of reaction system is 8.5, controlling temperature is 45 DEG C, and reacted serosity nature overflow is discharged in first order reaction still.
The mixed liquor of 1.5mol/L that Nickel dichloride., cobaltous chloride, manganese chloride are obtained according to the metal molar ratio than 0.50:0.20:0.30, the ammonium chloride solution of 3mol/L, 8mol/L sodium hydroxide solution simultaneously and flow in the first order reaction still adding stirring, reaction is at N2Carrying out under atmosphere protection, the control response time is 3h, and the pH value of reaction system solution is 11.2, and water bath heating temperature is 50 DEG C, and in spheroidal particle superficial growth, reacted one layer of cladding serosity overflows in secondary response still naturally.
By manganese chloride, the mixing salt solution of 1.5mol/L that magnesium sulfate obtains according to the metal molar ratio than 0.9:0.1,3mol/L sal volatile simultaneously and flow in the secondary response still adding stirring, the control response time is 2h, the pH value of reaction system solution is 9.0, water bath heating temperature is 50 DEG C, in spheroidal particle superficial growth, reacted two layers of cladding serosity overflow in third-order reaction still naturally.
The mixing salt solution of 1.5mol/L that magnesium chloride, aluminum chloride, zirconyl chloride obtained according to the metal molar ratio than 0.4:0.4:0.2,2mol/L ammonium hydrogen carbonate, 3mol/L sodium bicarbonate solution simultaneously and flow in the third-order reaction still adding stirring, the control response time is 1h, the pH value of the solution of reaction system is 8.8, water bath heating temperature is 50 DEG C, in spheroidal particle superficial growth, reacted three layers cladding serosity overflows in fourth-order reaction still naturally, through precipitation, washing, dry, obtain the spherical precursor material of three layers clad structure.By above-mentioned persursor material and lithium nitrate mix, under oxygen atmosphere, 930 DEG C of sintering 20h, prepare the anode material for lithium-ion batteries of three layers clad structure, testing this positive electrode meso-position radius is 7.1mm.
Embodiment 4
Nickel sulfate, cobaltous sulfate are dissolved according to the metal molar ratio than 0.9:0.1 and obtains the mixing salt solution of 1.8mol/L, the sodium hydroxide solution of 5mol/L, 12mol/L ammonia and simultaneously and flow in the nucleation reactor adding stirring, the control response time is 13h, the pH value of reaction system solution is 12.5, controlling temperature is 55 DEG C, and precipitation nature overflows in first order reaction still.
By 3mol/L cobalt chloride solution, the hydrogen peroxide of 3mol/L, 5mol/L potassium hydroxide solution simultaneously and flow in the first order reaction still adding stirring, the control response time is 8h, the pH value of reaction system solution is 9.0, it is 60 DEG C that heating in water bath controls temperature, and reacted one layer of serosity overflows in secondary response still naturally.
The Fluorinse of 1.0mol/L aluminum sulfate solution, 1mol/L simultaneously and is flowed in the secondary response still adding stirring, the control response time is 7h, the pH value of reaction system solution is 7.8, it is 60 DEG C that heating in water bath controls temperature, reacted two layers of cladding serosity, through precipitation, washing, dry, obtain the spherical precursor material of two layers of clad structure.By above-mentioned persursor material and lithium carbonate mix, in air atmosphere, 990 DEG C of sintering 10h, prepare the anode material for lithium-ion batteries of two layers of clad structure, testing this positive electrode meso-position radius is 10.2mm.
Embodiment 5
nullBy nickel sulfate、Cobaltous sulfate、Aluminum sulfate dissolves the mixing salt solution obtaining 1.8mol/L according to the metal molar ratio than 0.8:0.17:0.03、The EDTA solution of 1mol/L、The ammonia of 5mol/L、5mol/L sodium hydroxide solution and flows in the nucleation reactor adding stirring simultaneously,The control response time is 25h,The pH value of reaction system solution is 11.5,It is 50 DEG C that heating in water bath controls temperature,Reacted serosity is made naturally to overflow in first order reaction still,The phosphoric acid ammonia solution of the aluminum nitrate solution of 1mol/L with 1mol/L and is flowed in the first order reaction still adding stirring simultaneously,The control response time is 18h,The pH value of reaction system solution is 9,It is 50 DEG C that heating in water bath controls temperature,In core surface cladding growth,By material filtering after reaction、Washing、Dry,Obtain the spherical precursor material of one layer of cladding.By above-mentioned persursor material and Lithium hydrate mix, under oxygen atmosphere, 850 DEG C of sintering 12h, prepare the anode material for lithium-ion batteries of one layer of clad structure, testing this positive electrode meso-position radius is 13.5mm.
Embodiment 6
The nickel sulfate solution of 1.5mol/L, the sodium hydroxide solution of 10mol/L, 2mol/L ammonium sulfate simultaneously and are flowed in the nucleation reactor adding stirring, the control response time is 16h, the pH value of the solution of reaction system is 12.9, controlling temperature is 65 DEG C, and reacted serosity nature overflow is discharged in first order reaction still.
Cobaltous chloride, magnesium chloride, aluminum chloride are dissolved the mixing salt solution obtaining 1.5mol/L according to the metal molar ratio than 0.9:0.05:0.05, by mixing salt solution, the sodium hypochlorite of 1mol/L, 5mol/L sodium hydroxide solution simultaneously and flow in the first order reaction still adding stirring, the control response time is 10h, the pH value of reaction system solution is 9.5, it is 65 DEG C that heating in water bath controls temperature, in core surface cladding growth, by material filtering, washing, drying after reaction, obtain the spherical precursor material of one layer of cladding.By above-mentioned persursor material and lithium carbonate mix, in air atmosphere, 980 DEG C of sintering 15h, prepare the anode material for lithium-ion batteries of one layer of clad structure, testing this positive electrode meso-position radius is 4.2mm.

Claims (6)

1. a preparation method for the anode material for lithium-ion batteries of multilayer coating structure, is made up of following steps:
(1) continue to be injected in nucleation reactor (0) by nucleation reaction solution with liquid phase deposition, control response time 5 ~ 30h, make reacted serosity naturally overflow in first order reaction still (1);
(2) being continued by coating solution and stream is injected in first order reaction still (1), control coating response time 1 ~ 30h, reacted serosity overflows in secondary response still (2) naturally;
(3) serosity after ageing, by material filtering, dries, obtains the spherical precursor material of one layer of cladding in secondary response still (2);
When being coated with number of plies n > 1,
(4) n order reaction still serosity is constantly to n+1 order reaction still overflow, is continued by coating solution and stream is injected in n+1 order reaction still, controls response time 1 ~ 30h, and reacted serosity overflows in n+2 order reaction still naturally;Serosity after ageing, by material filtering, dries, obtains the spherical precursor material of n layer clad structure in n+2 order reaction still;
(5) by above-mentioned persursor material and lithium salts mix, under air or oxygen atmosphere, sintering prepares the anode material for lithium-ion batteries of multilayer coating structure.
2. the preparation method of the anode material for lithium-ion batteries of multilayer coating structure according to claim 1, it is characterised in that the scope of described anode material for lithium-ion batteries meso-position radius is 3 ~ 25 μm.
3. the preparation method of the anode material for lithium-ion batteries of multilayer coating structure according to claim 1, it is characterised in that in described step (1), nucleating solution is metal mixed saline solution with coating solution in step (2), (4), and it consists of NixM1-x, wherein 0.5≤x≤1.0 in step (1), 0≤x≤0.5 in step (2), (4), one or more in Co, Mn, Fe, Mg, Ca, Sr, Ba, B, Al, Y, Sm, Ti, Zn, Zr, Nb, Mo or W of M.
4. the preparation method of the anode material for lithium-ion batteries of multilayer coating structure according to claim 3, it is characterised in that described metal mixed saline solution is a kind of or wherein several mixture in sulfate, chlorate, nitrate, acetate or alkoxide.
5. the preparation method of the anode material for lithium-ion batteries of multilayer coating structure according to claim 1, it is characterized in that in described step (1), nucleating solution also includes precipitant with coating solution in step (2), (4), precipitant is a kind of or wherein several mixture in sodium hydroxide, potassium hydroxide, Lithium hydrate, sodium dihydrogen phosphate, disodium hydrogen phosphate, potassium dihydrogen phosphate, dipotassium hydrogen phosphate, ammonium phosphate, ammonium hydrogen carbonate, ammonium carbonate, sodium bicarbonate, sodium carbonate, potassium carbonate, sodium fluoride, ammonium fluoride.
6. the preparation method of the sphere material of multilayer coating structure according to claim 1, it is characterized in that in described step (1), in nucleating solution and step (2), (4), coating solution also includes reaction promoter solution, reaction promoter is a kind of in EDTA, ammonia, ammonium chloride, ammonium sulfate, ammonium nitrate, air, oxygen, ozone, hydrogen peroxide, sodium hypochlorite, sodium peroxydisulfate, nitrogen or wherein several nonreactive mixture.
CN201410848430.9A 2014-12-31 2014-12-31 Multilayer coated structure lithium ion battery positive electrode material preparation method Pending CN105810894A (en)

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Cited By (8)

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CN109428066A (en) * 2017-08-30 2019-03-05 中国科学院宁波材料技术与工程研究所 Core-shell material and preparation method thereof, lithium ion battery negative material and lithium ion battery
CN109428060A (en) * 2017-08-28 2019-03-05 中国科学院宁波材料技术与工程研究所 A kind of preparation method and application of cladded type multilayer presoma
CN109473667A (en) * 2017-10-23 2019-03-15 北京当升材料科技股份有限公司 Lithium ion battery presoma, positive electrode and preparation method thereof
CN110224137A (en) * 2019-05-28 2019-09-10 中南大学 A method of orientation constructs manganese containing materials interface-modifying layer
CN110534731A (en) * 2019-09-11 2019-12-03 李旭意 A kind of preparation method of gradient tertiary cathode material
CN112713263A (en) * 2020-12-14 2021-04-27 宁波维科新能源科技有限公司 Preparation method of metaphosphate coated lithium cobaltate material and lithium ion battery comprising metaphosphate coated lithium cobaltate material
CN113387400A (en) * 2021-05-26 2021-09-14 江苏集萃安泰创明先进能源材料研究院有限公司 Continuous production method and device for in-situ doping of high-nickel ternary cathode material precursor of lithium ion battery
CN114349069A (en) * 2021-12-03 2022-04-15 宜宾光原锂电材料有限公司 High-nickel ternary positive electrode material precursor and preparation method thereof

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CN102339984A (en) * 2010-07-28 2012-02-01 北京当升材料科技股份有限公司 Preparation method of spherical material with multilayer coating structure
CN103904318A (en) * 2012-12-28 2014-07-02 惠州比亚迪电池有限公司 Lithium battery positive electrode material and preparation method thereof

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CN102339984A (en) * 2010-07-28 2012-02-01 北京当升材料科技股份有限公司 Preparation method of spherical material with multilayer coating structure
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CN109428060A (en) * 2017-08-28 2019-03-05 中国科学院宁波材料技术与工程研究所 A kind of preparation method and application of cladded type multilayer presoma
CN109428066A (en) * 2017-08-30 2019-03-05 中国科学院宁波材料技术与工程研究所 Core-shell material and preparation method thereof, lithium ion battery negative material and lithium ion battery
CN109473667A (en) * 2017-10-23 2019-03-15 北京当升材料科技股份有限公司 Lithium ion battery presoma, positive electrode and preparation method thereof
CN109473667B (en) * 2017-10-23 2020-06-02 北京当升材料科技股份有限公司 Precursor for lithium ion battery, positive electrode material and preparation method of precursor
CN110224137A (en) * 2019-05-28 2019-09-10 中南大学 A method of orientation constructs manganese containing materials interface-modifying layer
CN110224137B (en) * 2019-05-28 2022-06-24 中南大学 Method for directionally constructing interface modification layer of manganese-containing material
CN110534731A (en) * 2019-09-11 2019-12-03 李旭意 A kind of preparation method of gradient tertiary cathode material
CN112713263A (en) * 2020-12-14 2021-04-27 宁波维科新能源科技有限公司 Preparation method of metaphosphate coated lithium cobaltate material and lithium ion battery comprising metaphosphate coated lithium cobaltate material
CN112713263B (en) * 2020-12-14 2021-12-28 宁波维科新能源科技有限公司 Preparation method of metaphosphate coated lithium cobaltate material and lithium ion battery comprising metaphosphate coated lithium cobaltate material
CN113387400A (en) * 2021-05-26 2021-09-14 江苏集萃安泰创明先进能源材料研究院有限公司 Continuous production method and device for in-situ doping of high-nickel ternary cathode material precursor of lithium ion battery
CN113387400B (en) * 2021-05-26 2023-09-05 江苏集萃安泰创明先进能源材料研究院有限公司 Continuous production method and device for in-situ doping of high-nickel ternary positive electrode material precursor of lithium ion battery
CN114349069A (en) * 2021-12-03 2022-04-15 宜宾光原锂电材料有限公司 High-nickel ternary positive electrode material precursor and preparation method thereof

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