WO2018126970A1 - Method for preparing lithium-ion battery slurry - Google Patents

Method for preparing lithium-ion battery slurry Download PDF

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Publication number
WO2018126970A1
WO2018126970A1 PCT/CN2017/119058 CN2017119058W WO2018126970A1 WO 2018126970 A1 WO2018126970 A1 WO 2018126970A1 CN 2017119058 W CN2017119058 W CN 2017119058W WO 2018126970 A1 WO2018126970 A1 WO 2018126970A1
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Prior art keywords
mixing
minutes
active material
speed
stirring
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PCT/CN2017/119058
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French (fr)
Chinese (zh)
Inventor
赖真龙
武永强
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深圳拓邦新能源技术有限公司
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Publication of WO2018126970A1 publication Critical patent/WO2018126970A1/en

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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/48Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/50Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese
    • H01M4/505Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese of mixed oxides or hydroxides containing manganese for inserting or intercalating light metals, e.g. LiMn2O4 or LiMn2OxFy
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • H01M10/0525Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/058Construction or manufacture
    • H01M10/0587Construction or manufacture of accumulators having only wound construction elements, i.e. wound positive electrodes, wound negative electrodes and wound separators
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/04Processes of manufacture in general
    • H01M4/0402Methods of deposition of the material
    • H01M4/0404Methods of deposition of the material by coating on electrode collectors
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/48Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/52Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron
    • H01M4/525Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron of mixed oxides or hydroxides containing iron, cobalt or nickel for inserting or intercalating light metals, e.g. LiNiO2, LiCoO2 or LiCoOxFy
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/58Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
    • H01M4/5825Oxygenated metallic salts or polyanionic structures, e.g. borates, phosphates, silicates, olivines
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/58Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
    • H01M4/583Carbonaceous material, e.g. graphite-intercalation compounds or CFx
    • 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
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

Definitions

  • the present invention relates to the field of lithium ion battery technology, and more particularly to a method of preparing a lithium ion battery slurry.
  • Lithium-ion battery is the best choice for mobile equipment and automotive power supply because of its advantages of light weight, large energy storage, high power, no pollution, long life, small self-discharge coefficient and wide temperature adaptation range. The prospects are very broad.
  • a lithium ion battery is obtained by winding a positive and negative electrode sheet and a separator into a battery, and then charging the electrolyte after being placed in a casing.
  • the positive and negative electrode sheets are obtained by dispersing the active material of the positive and negative electrodes in a solvent to form a slurry, and uniformly applying the slurry to the current collector for drying.
  • the slurry contains not only the positive and negative active materials, but also other powder excipients such as a binder, a conductive agent, and a thickener. The characteristics of each material are different, and the process of mixing them with the liquid is as follows. Question:
  • the technical problem to be solved by the present invention is to provide a preparation of a lithium ion battery slurry which is uniformly mixed and can efficiently prepare a battery slurry having good dispersibility and stability in view of the above-mentioned drawbacks of the prior art. method.
  • the technical solution adopted by the present invention to solve the technical problem thereof is: constructing a preparation method of a lithium ion battery slurry, comprising the following steps: [0010] Sl, mixing the active material and the auxiliary agent at a low speed to form a mixed powder;
  • the step S3 comprises: adding the remaining solvent to the mixture, using a shifting and reversing agitation under vacuum to uniformly mix, adding a styrene-butadiene rubber solution, low speed Stir for 30 minutes to form a lithium ion battery slurry.
  • step S3 the variable speed stirring speed is from 0r/mi n to 40r /min, and the forward and reverse conversion to the stirring period is 2 to 10 minutes; the low speed is 10 to 20r. /min.
  • the active material is a positive electrode active material or a negative electrode active material
  • the auxiliary agent includes a binder and a conductive agent
  • the solvent is N-methylpyrrolidone or deionized. water.
  • the positive active material is LiNi x M ni — x 0 2 , LiCo0 2
  • the negative active material is one or more of artificial graphite, natural graphite, and mesocarbon microbeads.
  • the binder is one or more of polyvinylidene fluoride, polytetrafluoroethylene, acrylate, polyurethane, sodium carboxymethylcellulose;
  • the conductive agent is one or more of conductive carbon black, conductive graphite, and carbon fiber.
  • step S1 the mixing time is 10 to 30 minutes, and the low speed is 1
  • step S3 the stirred and dispersed crucible is 30 to 120 minutes, and the vacuum degree in the vacuum state is -0.090 MPa to -0.1 MPa.
  • step S2 the total amount of the solvent added is 10 ⁇ 3 ⁇ 4 ⁇ 60 ⁇ 3 ⁇ 4 of the active material, and 30 ⁇ 120 minutes between the mixed turns.
  • step S2 the variable speed stirring speed is from 0 r/mi n to 40 r /min, and the forward and reverse conversion to the stirring period is 2 to 10 minutes.
  • step S3 the variable speed stirring speed is from 0 r/mi n to 40 r /min, and the forward-reverse conversion to the stirring period is 2 to 10 minutes.
  • the beneficial effects of the invention In the stirring process, the shifting and the commutating stirring can be used to quickly mix the raw materials uniformly, and the lithium ion battery slurry with good dispersibility and stability can be prepared with high efficiency, and the principle of chaotic mixing is utilized.
  • the mixing efficiency is improved, the mixing and mixing time is shortened, and the mixing uniformity is improved, so that the energy consumption in the production process is low, the production efficiency is improved, and the production cost is lowered.
  • FIG. 1 is a flow chart of a first embodiment of a method for preparing a lithium ion battery slurry of the present invention
  • FIG. 2 is a flow chart of a second embodiment of a method for preparing a lithium ion battery slurry of the present invention.
  • the present invention discloses a method for preparing a lithium ion battery slurry, which adopts a method of shifting and reversing agitation in a stirring process to rapidly mix raw materials uniformly, and can efficiently prepare a dispersion with high efficiency.
  • the lithium ion battery slurry of the nature and stability utilizes the principle of chaotic mixing to improve the mixing efficiency, shorten the mixing and mixing time, and improve the mixing uniformity, so that the energy consumption in the production process is low and the production efficiency is improved. , production costs are reduced.
  • a method for preparing a lithium ion battery slurry of the present invention comprises the following steps:
  • step Sl mixing the active material and the auxiliary agent at a low speed to form a mixed powder.
  • the mixing time is 10 ⁇ 30 minutes, and the low speed is 10 ⁇ 20r/min.
  • the mixing mode is not limited, and can be selected according to actual needs.
  • the mixed powder of step S1 is formed by mixing at a low speed in a dual planetary mixer.
  • the active material is a positive electrode active material or a negative electrode active material
  • the auxiliary agent includes a binder and a conductive agent.
  • the positive electrode active material is one or more of LiNi x Mn x 0 2 , LiCoO 2 , LiCo ( x+y )Ni x Mn y O 2 , Li 2 MnO 4 , LiFeP0 4 , wherein x, y, x+ y is greater than 0 and less than 1. Further, the positive electrode The active material is preferably one or more of Li 2 Mn 04 , LiFeP 04 , and LiCo 02 .
  • the anode active material is one or more of artificial graphite, natural graphite, and mesocarbon microbeads. It is preferably artificial graphite or natural graphite.
  • the binder is one or more of polyvinylidene fluoride, polytetrafluoroethylene, acrylate, polyurethane, sodium carboxymethylcellulose, vinylidene fluoride, hexafluoropropylene, preferably polycondensation One or two of vinyl fluoride and sodium carboxymethyl cellulose.
  • the conductive agent is one or more of conductive carbon black, conductive graphite, and carbon fiber, and is preferably one or both of conductive carbon black and conductive graphite.
  • the mixing time is 30 to 120 minutes. Further, the mixing time is preferably 60 to 90 minutes. Further, the mixing time is preferably 75 to 80 minutes.
  • the variable speed stirring speed is from 0r/mi n ⁇ 40r/min, and the forward and reverse conversion to the stirring period is 2 ⁇ 10 minutes. Further, the variable speed stirring speed is preferably from 0 r/mi n to 30 r /min, and the forward-reverse conversion to the stirring period is preferably 5 to 7 minutes.
  • the agitation mixing in the step S2 may be referred to as kneading, and the amount of the solvent may be appropriately added according to the solid content requirement, and may be selected according to actual needs to satisfy the viscosity requirement of the final slurry.
  • the solvent is N-methylpyrrolidone or deionized water.
  • the active material is a positive electrode active material ⁇
  • the solvent is preferably N-methylpyrrolidone
  • the active material is a negative electrode active material ⁇
  • the solvent is preferably deionized water.
  • the total amount of the solvent added in step S2 is 10 ⁇ 3 ⁇ 4 to 60% of the active material.
  • the amount of the solvent added is preferably from 30% to 50% of the active material. Further, the amount of the solvent added is preferably ⁇ SO ⁇ of the active material.
  • step S3 adding the remaining solvent to the mixture, and uniformly dispersing and dispersing in a vacuum state by using a shifting and forward-reverse conversion to form a lithium ion battery slurry.
  • the amount of the remaining solvent to be added is not particularly limited, and may be appropriately added depending on the solid content requirement.
  • the stirred and dispersed crucible is 30 to 120 minutes, and the vacuum degree in a vacuum state is -0.090 MPa to - 0.1 Mpa. Further, the mixing time is preferably 60 to 90 minutes. Further, the mixing time is preferably 75 to 80 minutes.
  • the speed of the variable speed stirring is from 0r/mi n to 40r /min, preferably from 0r/mi n to 30r /min.
  • the period of the forward-reverse conversion to the stirring is 2 to 10 minutes, preferably 5 to 7 minutes. .
  • the linear velocity of the agitation dispersion in step S3 is 5 to 25 m/s. Further, the dispersion linear velocity is preferably 10 to 20 m/s. Further, the dispersion linear velocity is preferably 15 to 20 m/s.
  • step S3 when preparing a lithium ion battery negative electrode slurry, step S3 includes: adding the remaining solvent to the mixture In the combined material, the shifting and reversing agitation were carried out under vacuum to uniformly mix, and a styrene butadiene rubber (SBR) solution was added, and the mixture was stirred at a low speed in the forward or reverse direction for 30 minutes to form a lithium ion battery slurry.
  • SBR styrene butadiene rubber
  • the variable speed stirring speed is from 0r/mi n to 40r/min, and the forward and reverse conversion to the stirring period is 2 to 10 minutes; the low speed is 10 to 20r/min, and the vacuum degree in the vacuum state is -0.090MPa ⁇ 0.1 Mpa.
  • the amount of the raw materials such as the binder, the conductive agent, and the lithium iron phosphate powder is weighed according to the ratio of the raw materials of the positive electrode slurry, and can be achieved by setting the ratio in the prior art.
  • a lithium ion battery positive electrode slurry can be prepared, and the lithium ion battery positive electrode slurry can be used to form a pole piece as a positive electrode of a lithium ion battery.
  • the lithium ion battery negative electrode slurry can be prepared when the active material used is a negative electrode active material, and the lithium ion battery negative electrode slurry can be used to form a pole piece as a negative electrode piece of a lithium ion battery.
  • the pole piece was fabricated, and the lithium ion battery slurry prepared above was coated on an aluminum foil and dried.
  • the positive electrode sheet and the negative electrode sheet and the separator are stacked and wound into a core, and the core is placed in an aluminum shell, and an electrolyte is injected and sealed to obtain a lithium ion battery.
  • Example 2 [0049] setting each of the following represents lOOOOg;

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Crystallography & Structural Chemistry (AREA)
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Abstract

The present invention relates to a method for preparing lithium-ion battery slurry, comprising the following steps: S1, mixing an active material and an auxiliary at low speed to form mixed powder; S2, adding part of a solvent into the mixed powder, and performing variable-speed and positive-negative rotation reversing stirring for uniform mixing to form a mixed material; S3, adding the remaining solvent into the mixed material, and performing variable-speed and positive-negative rotation reversing stirring under the vacuum state for uniform dispersing to form lithium-ion battery slurry. According to the present invention, in the stirring process, performing variable-speed and reversing stirring can quickly mix raw materials uniformly; and according to a chaotic mixing principle, the mixing efficiency is improved, and the purposes of shortening the mixing and stirring time and improving the mixing uniformity are achieved, the energy consumption is reduced and the production efficiency is improved in the production process, and production costs are reduced.

Description

一种锂离子电池浆料的制备方法 技术领域  Method for preparing lithium ion battery slurry
[0001] 本发明涉及锂离子电池技术领域, 更具体地说, 涉及一种锂离子电池浆料的制 备方法。  [0001] The present invention relates to the field of lithium ion battery technology, and more particularly to a method of preparing a lithium ion battery slurry.
背景技术  Background technique
[0002] 锂离子电池由于其具有重量轻、 储能大、 功率大、 无污染、 寿命长、 自放电系 数小以及温度适应范围广等突出的优点, 是移动设备和汽车动力电源最好的选 择, 前景十分广阔。  [0002] Lithium-ion battery is the best choice for mobile equipment and automotive power supply because of its advantages of light weight, large energy storage, high power, no pollution, long life, small self-discharge coefficient and wide temperature adaptation range. The prospects are very broad.
[0003] 锂离子电池是由正负极片和隔离膜卷绕成电芯后, 装入壳体后充入电解液后得 到的。 而正负极片是将正负极的活性材料分散在溶剂中形成浆料后, 把浆料均 匀的涂覆到集流体上进行烘干而得到的。 这种浆料不仅只有正负极活性物质, 还包含了粘结剂、 导电剂、 增稠剂等其他粉体辅料, 每种材料的特性不一, 将 他们与液体混合均匀的过程, 存在以下问题:  [0003] A lithium ion battery is obtained by winding a positive and negative electrode sheet and a separator into a battery, and then charging the electrolyte after being placed in a casing. On the other hand, the positive and negative electrode sheets are obtained by dispersing the active material of the positive and negative electrodes in a solvent to form a slurry, and uniformly applying the slurry to the current collector for drying. The slurry contains not only the positive and negative active materials, but also other powder excipients such as a binder, a conductive agent, and a thickener. The characteristics of each material are different, and the process of mixing them with the liquid is as follows. Question:
[0004] 1.粉体很难均匀的分散到液体溶剂中;  [0004] 1. The powder is difficult to uniformly disperse into the liquid solvent;
[0005] 2.粉体在溶剂中很难保持长吋间的悬浮稳定性;  [0005] 2. The powder is difficult to maintain the suspension stability between long turns in a solvent;
[0006] 3.搅拌吋间长, 设备能耗高;  [0006] 3. The mixing time is long, and the energy consumption of the equipment is high;
[0007] 4.设备利用率低。  [0007] 4. Equipment utilization is low.
技术问题 technical problem
[0008] 本发明要解决的技术问题在于, 针对现有技术的上述缺陷, 提供一种混合均匀 、 能高效率地制备具有良好分散性和稳定性的电池浆料的锂离子电池浆料的制 备方法。  [0008] The technical problem to be solved by the present invention is to provide a preparation of a lithium ion battery slurry which is uniformly mixed and can efficiently prepare a battery slurry having good dispersibility and stability in view of the above-mentioned drawbacks of the prior art. method.
问题的解决方案  Problem solution
技术解决方案  Technical solution
[0009] 本发明解决其技术问题所采用的技术方案是: 构造一种锂离子电池浆料的制备 方法, 包括以下步骤: [0010] Sl、 将活性材料和助剂低速混合形成混合粉体; [0009] The technical solution adopted by the present invention to solve the technical problem thereof is: constructing a preparation method of a lithium ion battery slurry, comprising the following steps: [0010] Sl, mixing the active material and the auxiliary agent at a low speed to form a mixed powder;
[0011] S2、 在所述混合粉体中加入部分溶剂, 采用变速和正反转换向搅拌, 混合均匀 [0011] S2, adding a part of the solvent to the mixed powder, using a shifting and forward-reverse conversion to stir, mixing evenly
, 形成混合物料; Forming a mixture;
[0012] S3、 将剩余的溶剂加入所述混合物料中, 真空状态下采用变速和正反转换向搅 拌分散均匀, 形成锂离子电池浆料。  [0012] S3, adding the remaining solvent to the mixture, and uniformly dispersing and dispersing in a vacuum state by using a shifting and forward-reverse conversion to form a lithium ion battery slurry.
[0013] 在本发明所述的制备方法中, 所述步骤 S3包括: 将剩余的溶剂加入所述混合物 料中, 真空状态下采用变速和换向搅拌以混合均匀, 加入丁苯橡胶溶液, 低速 搅拌 30分钟, 形成锂离子电池浆料。 [0013] In the preparation method of the present invention, the step S3 comprises: adding the remaining solvent to the mixture, using a shifting and reversing agitation under vacuum to uniformly mix, adding a styrene-butadiene rubber solution, low speed Stir for 30 minutes to form a lithium ion battery slurry.
[0014] 在本发明所述的制备方法中, 步骤 S3中, 变速搅拌速度从 0r/min~40r/min, 正 反转换向搅拌周期为 2~10分钟; 所述低速为 10~20r/min。 [0014] In the preparation method of the present invention, in step S3, the variable speed stirring speed is from 0r/mi n to 40r /min, and the forward and reverse conversion to the stirring period is 2 to 10 minutes; the low speed is 10 to 20r. /min.
[0015] 在本发明所述的制备方法中, 所述活性材料为正极活性材料或负极活性材料, 所述助剂包括粘结剂和导电剂, 所述溶剂为 N-甲基吡咯烷酮或去离子水。 [0015] In the preparation method of the present invention, the active material is a positive electrode active material or a negative electrode active material, the auxiliary agent includes a binder and a conductive agent, and the solvent is N-methylpyrrolidone or deionized. water.
[0016] 在本发明所述的制备方法中, 所述正极活性材料为 LiNi xMn ix0 2、 LiCo0 2 [0016] In the preparation method of the present invention, the positive active material is LiNi x M nix 0 2 , LiCo0 2
、 LiCo !_(x+y)Ni xMn yO 2、 Li 2MnO 4、 LiFePO 4 , LiCo !_ (x+y) Ni x Mn y O 2 , Li 2 MnO 4 , LiFePO 4
中的一种或多种, 其中, x、 y、 x+y均小于 1 ; 所述负极活性材料为人造石墨、 天然石墨、 中间相碳微球中的一种或多种。  One or more of them, wherein x, y, x+y are all less than 1; and the negative active material is one or more of artificial graphite, natural graphite, and mesocarbon microbeads.
[0017] 在本发明所述的制备方法中, 所述粘结剂为聚偏氟乙烯、 聚四氟乙烯、 丙烯酸 酯、 聚氨酯、 羧甲基纤维素钠中的一种或多种; 所述导电剂为导电炭黑、 导电 石墨、 碳纤维中的一种或多种。 [0017] In the preparation method of the present invention, the binder is one or more of polyvinylidene fluoride, polytetrafluoroethylene, acrylate, polyurethane, sodium carboxymethylcellulose; The conductive agent is one or more of conductive carbon black, conductive graphite, and carbon fiber.
[0018] 在本发明所述的制备方法中, 步骤 S1中, 混合吋间为 10~30分钟, 所述低速为 1[0018] In the preparation method of the present invention, in step S1, the mixing time is 10 to 30 minutes, and the low speed is 1
0~20r/min; 步骤 S3中, 搅拌分散的吋间为 30~120分钟, 所述真空状态的真空度 为 -0.090MPa~ -0.1 MPa。 0~20r/min; In step S3, the stirred and dispersed crucible is 30 to 120 minutes, and the vacuum degree in the vacuum state is -0.090 MPa to -0.1 MPa.
[0019] 在本发明所述的制备方法中, 步骤 S2中, 所述溶剂的添加总量为所述活性材料 的 10<¾~60<¾, 混合吋间为 30~120分钟。 In the preparation method of the present invention, in step S2, the total amount of the solvent added is 10<3⁄4~60<3⁄4 of the active material, and 30~120 minutes between the mixed turns.
[0020] 在本发明所述的制备方法中, 步骤 S2中, 变速搅拌速度从 0r/min~40r/min, 正 反转换向搅拌周期为 2~10分钟。 [0020] In the preparation method of the present invention, in step S2, the variable speed stirring speed is from 0 r/mi n to 40 r /min, and the forward and reverse conversion to the stirring period is 2 to 10 minutes.
[0021] 在本发明所述的制备方法中, 步骤 S3中, 变速搅拌速度从 0r/min~40r/min, 正 反转换向搅拌周期为 2~10分钟。 发明的有益效果 [0021] In the preparation method of the present invention, in step S3, the variable speed stirring speed is from 0 r/mi n to 40 r /min, and the forward-reverse conversion to the stirring period is 2 to 10 minutes. Advantageous effects of the invention
有益效果  Beneficial effect
[0022] 本发明的有益效果: 搅拌过程中采用变速和换向搅拌能快速地将原料混合均匀 , 能高效率的制备具有良好分散性和稳定性的锂离子电池浆料, 利用混沌混合 的原理, 提高了混合的效率, 达到缩短混合搅拌吋间、 提高混合均匀度的目的 , 使得生产过程中能耗消耗低、 生产效率提高, 生产成本降低。  [0022] The beneficial effects of the invention: In the stirring process, the shifting and the commutating stirring can be used to quickly mix the raw materials uniformly, and the lithium ion battery slurry with good dispersibility and stability can be prepared with high efficiency, and the principle of chaotic mixing is utilized. The mixing efficiency is improved, the mixing and mixing time is shortened, and the mixing uniformity is improved, so that the energy consumption in the production process is low, the production efficiency is improved, and the production cost is lowered.
对附图的简要说明  Brief description of the drawing
附图说明  DRAWINGS
[0023] 下面将结合附图及实施例对本发明作进一步说明, 附图中:  [0023] The present invention will be further described below in conjunction with the accompanying drawings and embodiments, in which:
[0024] 图 1是本发明锂离子电池浆料的制备方法第一实施例的流程图; 1 is a flow chart of a first embodiment of a method for preparing a lithium ion battery slurry of the present invention;
[0025] 图 2是本发明锂离子电池浆料的制备方法第二实施例的流程图。 2 is a flow chart of a second embodiment of a method for preparing a lithium ion battery slurry of the present invention.
实施该发明的最佳实施例  BEST MODE FOR CARRYING OUT THE INVENTION
本发明的最佳实施方式  BEST MODE FOR CARRYING OUT THE INVENTION
[0026] 为了对本发明的技术特征、 目的和效果有更加清楚的理解, 现对照附图详细说 明本发明的具体实施方式。  The embodiments of the present invention will be described in detail with reference to the accompanying drawings.
[0027] 本发明公幵了一种锂离子电池浆料的制备方法, 该方法通过在搅拌过程中采用 变速和换向搅拌的方法从而快速地将原料混合均匀, 能高效率地制备具有良好 分散性和稳定性的锂离子电池浆料, 利用了混沌混合的原理, 提高了混合的效 率, 达到缩短混合搅拌吋间, 提高混合均匀度的目的, 使得生产过程中能耗消 耗低、 生产效率提高, 生产成本降低。  [0027] The present invention discloses a method for preparing a lithium ion battery slurry, which adopts a method of shifting and reversing agitation in a stirring process to rapidly mix raw materials uniformly, and can efficiently prepare a dispersion with high efficiency. The lithium ion battery slurry of the nature and stability utilizes the principle of chaotic mixing to improve the mixing efficiency, shorten the mixing and mixing time, and improve the mixing uniformity, so that the energy consumption in the production process is low and the production efficiency is improved. , production costs are reduced.
[0028] 参阅图 1, 本发明锂离子电池浆料的制备方法, 包括以下步骤:  [0028] Referring to FIG. 1, a method for preparing a lithium ion battery slurry of the present invention comprises the following steps:
[0029] Sl、 将活性材料和助剂低速混合形成混合粉体。 该步骤中, 混合吋间为 10~30 分钟, 所述低速为 10~20r/min, 混合的方式并不受到具体的限制, 可根据实际需 求进行选择。 优选地, 步骤 S1的混合粉体在双行星搅拌机中低速混合形成。  [0029] Sl, mixing the active material and the auxiliary agent at a low speed to form a mixed powder. In this step, the mixing time is 10~30 minutes, and the low speed is 10~20r/min. The mixing mode is not limited, and can be selected according to actual needs. Preferably, the mixed powder of step S1 is formed by mixing at a low speed in a dual planetary mixer.
[0030] 其中, 活性材料为正极活性材料或负极活性材料, 助剂包括粘结剂和导电剂。  [0030] wherein the active material is a positive electrode active material or a negative electrode active material, and the auxiliary agent includes a binder and a conductive agent.
正极活性材料为 LiNi xMn x0 2、 LiCoO 2、 LiCo (x+y)Ni xMn yO 2、 Li 2MnO 4 、 LiFeP0 4中的一种或多种, 其中, x、 y、 x+y均大于 0小于 1。 进一步地, 正极 活性材料优选为 Li2Mn04、 LiFeP04、 LiCo02中的一种或多种。 The positive electrode active material is one or more of LiNi x Mn x 0 2 , LiCoO 2 , LiCo ( x+y )Ni x Mn y O 2 , Li 2 MnO 4 , LiFeP0 4 , wherein x, y, x+ y is greater than 0 and less than 1. Further, the positive electrode The active material is preferably one or more of Li 2 Mn 04 , LiFeP 04 , and LiCo 02 .
[0031] 负极活性材料为人造石墨、 天然石墨、 中间相碳微球中的一种或多种。 优选为 人造石墨或天然石墨。  [0031] The anode active material is one or more of artificial graphite, natural graphite, and mesocarbon microbeads. It is preferably artificial graphite or natural graphite.
[0032] 粘结剂为聚偏氟乙烯、 聚四氟乙烯、 丙烯酸酯、 聚氨酯、 羧甲基纤维素钠、 偏 二氟乙烯、 六氟丙烯中的一种或多种, 优选地为聚偏氟乙烯、 羧甲基纤维素钠 中的一种或两种。 导电剂为导电炭黑、 导电石墨、 碳纤维中的一种或多种, 优 选地为导电炭黑、 导电石墨中的一种或两种。  [0032] The binder is one or more of polyvinylidene fluoride, polytetrafluoroethylene, acrylate, polyurethane, sodium carboxymethylcellulose, vinylidene fluoride, hexafluoropropylene, preferably polycondensation One or two of vinyl fluoride and sodium carboxymethyl cellulose. The conductive agent is one or more of conductive carbon black, conductive graphite, and carbon fiber, and is preferably one or both of conductive carbon black and conductive graphite.
[0033] S2、 在混合粉体中加入部分溶剂, 采用变速和正反转换向搅拌, 混合均匀, 形 成混合物料。 混合吋间为 30~120分钟。 进一步地, 混合吋间优选为 60~90分钟。 更进一步地, 混合吋间优选为 75~80分钟。 变速搅拌速度从 0r/min~40r/min, 正反 转换向搅拌周期为 2~10分钟。 进一步地, 变速搅拌速度优选为从 0r/min~30r/min , 正反转换向搅拌周期优选为 5~7分钟。 [0033] S2, a part of the solvent is added to the mixed powder, and the mixture is stirred and mixed uniformly by shifting and forward-reverse conversion to form a mixed material. The mixing time is 30 to 120 minutes. Further, the mixing time is preferably 60 to 90 minutes. Further, the mixing time is preferably 75 to 80 minutes. The variable speed stirring speed is from 0r/mi n ~40r/min, and the forward and reverse conversion to the stirring period is 2~10 minutes. Further, the variable speed stirring speed is preferably from 0 r/mi n to 30 r /min, and the forward-reverse conversion to the stirring period is preferably 5 to 7 minutes.
[0034] 该步骤 S2的搅拌混合可称为捏合, 溶剂的用量根据固含量要求适当添加, 可根 据实际需求进行选择, 满足最终浆料的粘度要求即可。 优选地, 溶剂为 N-甲基 吡咯烷酮或去离子水。 当活性材料为正极活性材料吋, 溶剂优选为 N-甲基吡咯 烷酮; 活性材料为负极活性材料吋, 溶剂优选为去离子水。  [0034] The agitation mixing in the step S2 may be referred to as kneading, and the amount of the solvent may be appropriately added according to the solid content requirement, and may be selected according to actual needs to satisfy the viscosity requirement of the final slurry. Preferably, the solvent is N-methylpyrrolidone or deionized water. When the active material is a positive electrode active material 吋, the solvent is preferably N-methylpyrrolidone; the active material is a negative electrode active material 吋, and the solvent is preferably deionized water.
[0035] 在优选的实施方式中, 步骤 S2中的溶剂的添加总量为活性材料的 10<¾~60%。  In a preferred embodiment, the total amount of the solvent added in step S2 is 10<3⁄4 to 60% of the active material.
进一步地, 溶剂的添加量优选为活性材料的 30%~50%。 更进一步地, 溶剂的添 加量优选为活性材料的 ^ SO^。  Further, the amount of the solvent added is preferably from 30% to 50% of the active material. Further, the amount of the solvent added is preferably ^ SO ^ of the active material.
[0036] S3、 将剩余的溶剂加入混合物料中, 真空状态下采用变速和正反转换向搅拌分 散均匀, 形成锂离子电池浆料。 该步骤 S3中, 加入的剩余溶剂量不受到具体限 制, 可根据固含量要求适当添加。 搅拌分散的吋间为 30~120分钟, 真空状态的 真空度为 -0.090MPa〜 - 0.1 Mpa。 进一步地, 混合吋间优选为 60~90分钟。 更进一 步地, 混合吋间优选为 75~80分钟。 变速搅拌的速度从 0r/min~40r/min, 优选为从 0r/min~30r/min。 正反转换向搅拌的周期为 2~10分钟, 优选为 5~7分钟。 。 [0036] S3, adding the remaining solvent to the mixture, and uniformly dispersing and dispersing in a vacuum state by using a shifting and forward-reverse conversion to form a lithium ion battery slurry. In the step S3, the amount of the remaining solvent to be added is not particularly limited, and may be appropriately added depending on the solid content requirement. The stirred and dispersed crucible is 30 to 120 minutes, and the vacuum degree in a vacuum state is -0.090 MPa to - 0.1 Mpa. Further, the mixing time is preferably 60 to 90 minutes. Further, the mixing time is preferably 75 to 80 minutes. The speed of the variable speed stirring is from 0r/mi n to 40r /min, preferably from 0r/mi n to 30r /min. The period of the forward-reverse conversion to the stirring is 2 to 10 minutes, preferably 5 to 7 minutes. .
[0037] 在优选的实施方式中, 步骤 S3中的搅拌分散的线速度为 5~25m/s。 进一步地, 分散线速度优选为 10~20m/s。 更进一步地, 分散线速度优选为 15~20m/s。  In a preferred embodiment, the linear velocity of the agitation dispersion in step S3 is 5 to 25 m/s. Further, the dispersion linear velocity is preferably 10 to 20 m/s. Further, the dispersion linear velocity is preferably 15 to 20 m/s.
[0038] 参阅图 2, 当制备锂离子电池负极浆料吋, 步骤 S3包括: 将剩余的溶剂加入混 合物料中, 真空状态下采用变速和换向搅拌以混合均匀, 加入丁苯橡胶 (SBR) 溶液, 正向或反向低速搅拌 30分钟, 形成锂离子电池浆料。 该步骤 S3中, 变速 搅拌速度从 0r/min~40r/min, 正反转换向搅拌周期为 2~10分钟; 低速为 10~20r/mi n, 真空状态的真空度为 -0.090MPa~ -0.1 Mpa。 [0038] Referring to FIG. 2, when preparing a lithium ion battery negative electrode slurry, step S3 includes: adding the remaining solvent to the mixture In the combined material, the shifting and reversing agitation were carried out under vacuum to uniformly mix, and a styrene butadiene rubber (SBR) solution was added, and the mixture was stirred at a low speed in the forward or reverse direction for 30 minutes to form a lithium ion battery slurry. In the step S3, the variable speed stirring speed is from 0r/mi n to 40r/min, and the forward and reverse conversion to the stirring period is 2 to 10 minutes; the low speed is 10 to 20r/min, and the vacuum degree in the vacuum state is -0.090MPa~ 0.1 Mpa.
[0039] 上述制备方法中, 粘结剂、 导电剂、 磷酸铁锂粉体等原料用量根据正极浆料各 原料配比称取, 可采用现有技术中所设定配比实现。  [0039] In the above preparation method, the amount of the raw materials such as the binder, the conductive agent, and the lithium iron phosphate powder is weighed according to the ratio of the raw materials of the positive electrode slurry, and can be achieved by setting the ratio in the prior art.
[0040] 采用本发明的的制备方法, 当使用的活性材料为正极活性材料吋可制备锂离子 电池正极浆料, 使用该锂离子电池正极浆料可制成极片, 作为锂离子电池的正 极片; 当使用的活性材料为负极活性材料吋可制备锂离子电池负极浆料, 使用 该锂离子电池负极浆料可制成极片, 作为锂离子电池的负极片。  [0040] By using the preparation method of the present invention, when the active material used is a positive electrode active material, a lithium ion battery positive electrode slurry can be prepared, and the lithium ion battery positive electrode slurry can be used to form a pole piece as a positive electrode of a lithium ion battery. The lithium ion battery negative electrode slurry can be prepared when the active material used is a negative electrode active material, and the lithium ion battery negative electrode slurry can be used to form a pole piece as a negative electrode piece of a lithium ion battery.
[0041] 极片制作吋, 将上述制得的锂离子电池浆料涂覆在铝箔上, 烘干后即得。  [0041] The pole piece was fabricated, and the lithium ion battery slurry prepared above was coated on an aluminum foil and dried.
[0042] 将正极片与负极片、 隔膜叠置后卷绕成卷芯, 将卷芯放入铝壳中, 注入电解液 , 封口, 制得锂离子电池。  [0042] The positive electrode sheet and the negative electrode sheet and the separator are stacked and wound into a core, and the core is placed in an aluminum shell, and an electrolyte is injected and sealed to obtain a lithium ion battery.
[0043] 下面将以具体实施例来对本发明进行说明。  [0043] The invention will now be described in the context of specific embodiments.
[0044] 下述实施例和对比例均在 DP-25型双行星搅拌机中完成型双行星搅拌机中进行  [0044] The following examples and comparative examples were carried out in a completed double planetary mixer in a DP-25 double planetary mixer.
[0045] 实施例 1 : [0045] Example 1 :
[0046] 设定以下每份代表 lOOOg;  [0046] setting each of the following representatives lOOOOg;
[0047] 取 2.5份 PVDF (聚偏氟乙烯) 、 2份 Super-P (导电炭黑)、 1份 KS-6 (导电石墨) 和 94.5份磷酸铁锂, 加入搅拌机中以 10r转速下均匀混合 20分钟形成混合粉体。 加入 47份 N-甲基吡咯烷酮, 搅拌从 Or/min加速到 30r/min, 匀速搅拌 5min, 停止搅 拌, 搅拌速度从 30r/min减速到 0r/min, 启动反转搅拌, 搅拌从 0r/min加速到 30r/m in, 匀速搅拌 5min, 如此循环。 过程中分散以 15m/s转速持续运行, 总吋间 80分 钟。 加入 53份 N-甲基吡咯烷酮后, 抽真空至 -0.095Mpa, 搅拌从 Or/min加速到 30r/ min, 匀速搅拌 5min, 停止搅拌, 搅拌速度从 30r/min减速到 Or/min, 启动反转搅 拌, 搅拌从 Or/min加速到 30r/min, 匀速搅拌 5min, 如此循环。 过程中分散以 15m/ s转速持续运行, 总吋间 80分钟, 形成锂离子电池正极浆料。  [0047] taking 2.5 parts of PVDF (polyvinylidene fluoride), 2 parts of Super-P (conductive carbon black), 1 part of KS-6 (conductive graphite) and 94.5 parts of lithium iron phosphate, added to the mixer and uniformly mixed at 10r rotation speed The mixed powder was formed in 20 minutes. Add 47 parts of N-methylpyrrolidone, accelerate from Or/min to 30r/min, stir at a constant speed for 5min, stop stirring, decelerate from 30r/min to 0r/min, start reverse mixing, and stir from 0r/min Stir at a constant speed for 5 min at 30 r/m in. During the process, the dispersion was continuously operated at a speed of 15 m/s for a total of 80 minutes. After adding 53 parts of N-methylpyrrolidone, evacuate to -0.095Mpa, stir from Or/min to 30r/min, stir at a constant speed for 5min, stop stirring, and the stirring speed is decelerated from 30r/min to Or/min. Stir, stir from Or/min to 30r/min, stir at a constant speed for 5min, and cycle. During the process, the dispersion was continuously operated at a speed of 15 m/s, and the total daytime was 80 minutes to form a positive electrode slurry of a lithium ion battery.
[0048] 实施例 2: [0049] 设定以下每份代表 lOOOg; Example 2: [0049] setting each of the following represents lOOOOg;
[0050] 取 1.5份 CMC (羧甲基纤维素钠) 、 1.5份 Super-P (导电炭黑)、 和 94.8份人造石 墨, 加入搅拌机中以 10r转速下均匀混合 30分钟形成混合粉体。 加入 48份去离子 水, 搅拌从 0r/min加速到 30r/min, 匀速搅拌 5min, 停止搅拌, 搅拌速度从 30r/mi n减速到 0r/min, 启动反转搅拌, 搅拌从 0r/min加速到 30r/min, 匀速搅拌 5min, 如此循环。 过程中分散以 18m/s转速持续运行, 总吋间 90分钟。 加入 52份去离子 水后, 抽真空至 -0.095Mpa, 搅拌从 0r/min加速到 30r/min, 匀速搅拌 5min, 停止 搅拌, 搅拌速度从 30r/min减速到 0r/min, 启动反转搅拌, 搅拌从 Or/min加速到 30r /min, 匀速搅拌 5min, 如此循环。 过程中分散以 18m/s转速持续运行, 总吋间 90 分钟。 加入 5份 SBR乳液, 以 25r/min搅拌, 5m/s线速度分散, 混合 30min, 形成 锂离子电池负极浆料。  [0050] 1.5 parts of CMC (carboxymethylcellulose sodium), 1.5 parts of Super-P (conductive carbon black), and 94.8 parts of artificial graphite were placed, and uniformly mixed at a rotational speed of 10 rpm for 30 minutes in a mixer to form a mixed powder. Add 48 parts of deionized water, stir from 0r/min to 30r/min, stir at a constant speed for 5min, stop stirring, decelerate from 30r/mi n to 0r/min, start reverse mixing, and accelerate from 0r/min to 30r/min, stir at a constant speed for 5min, and cycle. During the process, the dispersion was continuously run at 18 m/s for 90 minutes. After adding 52 parts of deionized water, evacuate to -0.095Mpa, stir from 0r/min to 30r/min, stir at a constant speed for 5min, stop stirring, decelerate from 30r/min to 0r/min, start reverse mixing. Stirring was accelerated from Or/min to 30 r / min, stirred at a constant rate for 5 min, and cycled. During the process, the dispersion was continuously operated at 18 m/s and the total time was 90 minutes. 5 parts of SBR emulsion was added, stirred at 25 r/min, dispersed at a line speed of 5 m/s, and mixed for 30 minutes to form a negative electrode slurry of a lithium ion battery.
[0051] 对比例 1 :  Comparative Example 1 :
[0052] 设定以下每份代表 lOOOg;  [0052] setting each of the following representatives lOOOOg;
[0053] 取 2.5份 PVDF (聚偏氟乙烯) 、 2份 Super-P (导电炭黑)、 1份 KS-6 (导电石墨) 和 94.5份磷酸铁锂, 加入搅拌机中以 10r转速下均匀混合 20分钟形成粉体。 加入 4 7份 N-甲基吡咯烷酮, 以搅拌速度 30r/min, 分散速度 15m/s转速持续搅拌, 总吋 间 120分钟。 加入 53份 N-甲基吡咯烷酮后, 抽真空至 -0.095Mpa, 以搅拌速度 30r/ min, 分散速度 15m/s转速持续搅拌, 总吋间 120分钟, 形成锂离子电池正极浆料 [0053] taking 2.5 parts of PVDF (polyvinylidene fluoride), 2 parts of Super-P (conductive carbon black), 1 part of KS-6 (conductive graphite) and 94.5 parts of lithium iron phosphate, added to the mixer and uniformly mixed at 10r rotation speed The powder was formed in 20 minutes. 47 parts of N-methylpyrrolidone was added, and the stirring was continued at a stirring speed of 30 r /min, and the stirring speed was 15 m/s, and the mixture was continuously stirred for 120 minutes. After adding 53 parts of N-methylpyrrolidone, vacuuming to -0.095Mpa, stirring at a rate of 30r/min, stirring at a speed of 15m/s, and stirring for a total of 120 minutes, forming a positive ion slurry of lithium ion battery
[0054] 对比例 2: Comparative Example 2:
[0055] 设定以下每份代表 1000g; [0055] setting the following representative to each 1000g ;
[0056] 取 1.5份 CMC (羧甲基纤维素钠) 、 1.5份 Super-P (导电炭黑)、 和 94.8份人造石 墨, 加入搅拌机中以 10r转速下均匀混合 30分钟形成粉体。 加入 48份去离子水, 以搅拌速度 30r/min, 分散速度 18m/s转速持续搅拌, 总吋间 150分钟。 加入 52份 去离子水后, 抽真空至 -0.095Mpa, 以搅拌速度 30r/min, 分散速度 18m/s转速持 续搅拌, 总吋间 150分钟。 加入 5份 SBR乳液, 以 25r/min搅拌, 5m/s线速度分散 , 混合 30min, 形成锂离子电池负极浆料。  [0056] 1.5 parts of CMC (carboxymethylcellulose sodium), 1.5 parts of Super-P (conductive carbon black), and 94.8 parts of artificial graphite were placed, and uniformly mixed for 30 minutes at a rotational speed of 10 rpm in a mixer to form a powder. 48 parts of deionized water was added, stirring was continued at a stirring speed of 30 r/min, and the stirring speed was maintained at a speed of 18 m/s for a total of 150 minutes. After adding 52 parts of deionized water, evacuate to -0.095 MPa, stirring at a rate of 30 r/min, and stirring at a speed of 18 m/s for a total of 150 minutes. 5 parts of SBR emulsion was added, stirred at 25 r/min, dispersed at a line speed of 5 m/s, and mixed for 30 minutes to form a negative electrode slurry of a lithium ion battery.
[0057] 实施例 1、 2和对比例 1、 2的总吋间统计和浆料测试结果如下表 1。 [0058] 表 1.总吋间统计和制得浆料测试结果 The total inter-turn statistics and slurry test results of Examples 1, 2 and Comparative Examples 1, 2 are shown in Table 1 below. Table 1. Total inter-day statistics and slurry test results
[] [表 1] [] [Table 1]
Figure imgf000009_0001
Figure imgf000009_0001
[0059] 从表 1所示的实验结果看, 实施例 1、 2的混料方法相比于传统 (比较例 1、 2) 的混料方法, 效果上差异不大, 但吋间明显要短 27%~31%, 效率提升和降低能 耗效果明显。  [0059] From the experimental results shown in Table 1, the mixing methods of Examples 1 and 2 have little difference in effect compared with the conventional (Comparative Examples 1 and 2) mixing methods, but are obviously shorter in the daytime. 27%~31%, the efficiency is improved and the energy consumption is reduced.
[0060] 可以理解的, 以上实施例仅表达了本发明的优选实施方式, 其描述较为具体和 详细, 但并不能因此而理解为对本发明专利范围的限制; 应当指出的是, 对于 本领域的普通技术人员来说, 在不脱离本发明构思的前提下, 可以对上述技术 特点进行自由组合, 还可以做出若干变形和改进, 这些都属于本发明的保护范 围; 因此, 凡跟本发明权利要求范围所做的等同变换与修饰, 均应属于本发明 权利要求的涵盖范围。  [0060] It is to be understood that the above embodiments are merely illustrative of the preferred embodiments of the present invention, and are not to be construed as limiting the scope of the invention; A person skilled in the art can freely combine the above technical features without departing from the inventive concept, and can also make several modifications and improvements, which are all within the scope of the present invention; therefore, the rights of the present invention Equivalent transformations and modifications made to the scope of the claims are intended to be included within the scope of the appended claims.

Claims

权利要求书 Claim
一种锂离子电池浆料的制备方法, 其特征在于, 包括以下步骤:A method for preparing a lithium ion battery slurry, comprising the steps of:
S 1、 将活性材料和助剂低速混合形成混合粉体; S1, mixing the active material and the auxiliary agent at a low speed to form a mixed powder;
52、 在所述混合粉体中加入部分溶剂, 采用变速和正反转换向搅拌, 混合均匀, 形成混合物料;  52, adding a part of the solvent to the mixed powder, using a shifting and forward-reverse conversion to stir, mixing uniformly to form a mixed material;
53、 将剩余的溶剂加入所述混合物料中, 真空状态下采用变速和正反 转换向搅拌分散均匀, 形成锂离子电池浆料。  53. The remaining solvent is added to the mixture, and the dispersion and dispersion are uniformly dispersed in a vacuum state by using a shifting and forward-reverse conversion to form a lithium ion battery slurry.
根据权利要求 1所述的制备方法, 其特征在于, 所述步骤 S3包括: 将 剩余的溶剂加入所述混合物料中, 真空状态下采用变速和换向搅拌以 混合均匀, 加入丁苯橡胶溶液, 低速搅拌 30分钟, 形成锂离子电池浆 料。 The preparation method according to claim 1, wherein the step S3 comprises: adding the remaining solvent to the mixture, and using a shifting and reversing agitation under vacuum to uniformly mix, adding a styrene-butadiene rubber solution, Stir at low speed for 30 minutes to form a lithium ion battery slurry.
根据权利要求 2所述的制备方法, 其特征在于, 步骤 S3中, 变速搅拌 速度从 0r/min~40r/min, 正反转换向搅拌周期为 2~10分钟; 所述低速 为 10~20r/min。 The preparation method according to claim 2, wherein in step S3, the variable speed stirring speed is from 0 r /mi n to 40 r /min, and the forward and reverse conversion to the stirring period is 2 to 10 minutes; ~20r/min.
根据权利要求 1所述的制备方法, 其特征在于, 所述活性材料为正极 活性材料或负极活性材料, 所述助剂包括粘结剂和导电剂, 所述溶剂 为 N-甲基吡咯烷酮或去离子水。 The preparation method according to claim 1, wherein the active material is a positive electrode active material or a negative electrode active material, and the auxiliary agent comprises a binder and a conductive agent, and the solvent is N-methylpyrrolidone or Ionic water.
根据权利要求 4所述的制备方法, 其特征在于, 所述正极活性材料为The method according to claim 4, wherein the positive active material is
LiNi xMn l x0 2、 LiCo0 2、 LiCo x+y)Ni xMn yO 2、 Li 2Mn0 4、 LiFePO 4 中的一种或多种, 其中, x、 y、 x+y均小于 1 ; 所述负极活性材料为 人造石墨、 天然石墨、 中间相碳微球中的一种或多种。 One or more of LiNi x Mn lx 0 2 , LiCo0 2 , LiCo x+y ) Ni x Mn y O 2 , Li 2 Mn0 4 , LiFePO 4 , wherein x, y, x+y are all less than 1; The negative active material is one or more of artificial graphite, natural graphite, and mesocarbon microbeads.
根据权利要求 4所述的制备方法, 其特征在于, 所述粘结剂为聚偏氟 乙烯、 聚四氟乙烯、 丙烯酸酯、 聚氨酯、 羧甲基纤维素钠中的一种或 多种; 所述导电剂为导电炭黑、 导电石墨、 碳纤维中的一种或多种。 根据权利要求 1所述的制备方法, 其特征在于, 步骤 S1中, 混合吋间 为 10~30分钟, 所述低速为 10~20r/min; 步骤 S3中, 混合吋间为 30~12The preparation method according to claim 4, wherein the binder is one or more of polyvinylidene fluoride, polytetrafluoroethylene, acrylate, polyurethane, sodium carboxymethylcellulose; The conductive agent is one or more of conductive carbon black, conductive graphite, and carbon fiber. The preparation method according to claim 1, wherein in step S1, the mixing time is 10 to 30 minutes, and the low speed is 10 to 20 r/min; in step S3, the mixing time is 30 to 12
0分钟, 所述真空状态的真空度为 -0.090MPa~ -0.1 MPa。 At 0 minutes, the vacuum in the vacuum state was -0.090 MPa to -0.1 MPa.
根据权利要求 1所述的制备方法, 其特征在于, 步骤 S2中, 所述溶剂 的添加总量为所述活性材料的 10%~60<¾, 搅拌分散的吋间为 30~120 分钟。 The preparation method according to claim 1, wherein in the step S2, the solvent The total amount of addition is 10%~60<3⁄4 of the active material, and the mixing and dispersing time is 30~120 minutes.
[权利要求 9] 根据权利要求 1所述的制备方法, 其特征在于, 步骤 S2中, 变速搅拌 速度从 0r/min~40r/min , 正反转换向搅拌周期为 2~ 10分钟。  [Claim 9] The preparation method according to claim 1, wherein in step S2, the variable speed stirring speed is from 0 r/min to 40 r/min, and the forward-reverse conversion to the stirring period is 2 to 10 minutes.
[权利要求 10] 根据权利要求 1所述的制备方法, 其特征在于, 步骤 S3中, 变速搅拌 速度从 0r/min~40r/min, 正反转换向搅拌周期为 2~ 10分钟。 [Claim 10] The preparation method according to claim 1, wherein in step S3, the variable speed stirring speed is from 0r/mi n to 40r/min, and the forward and reverse conversion to the stirring period is 2 to 10 minutes.
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