JP2017174804A - Aqueous binder for lithium ion battery negative electrode and preparation method of the same - Google Patents

Aqueous binder for lithium ion battery negative electrode and preparation method of the same Download PDF

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JP2017174804A
JP2017174804A JP2017027161A JP2017027161A JP2017174804A JP 2017174804 A JP2017174804 A JP 2017174804A JP 2017027161 A JP2017027161 A JP 2017027161A JP 2017027161 A JP2017027161 A JP 2017027161A JP 2017174804 A JP2017174804 A JP 2017174804A
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lithium ion
ion battery
aqueous binder
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強 李
Qiang Li
強 李
豊瑞 白
Fengrui Bai
豊瑞 白
賀斌 羅
Hebin Luo
賀斌 羅
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Blue Ocean & Black Stone Tech Co Ltd (fujian)
Blue Ocean & Black Stone Technology Co Ltd (fujian)
Blue Ocean & Black Stone Technology Co ltd Fujian
Blue Ocean & Black Stone Technology Co ltd(fujian)
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    • 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
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2/00Processes of polymerisation
    • C08F2/12Polymerisation in non-solvents
    • C08F2/16Aqueous medium
    • C08F2/22Emulsion polymerisation
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2/00Processes of polymerisation
    • C08F2/44Polymerisation in the presence of compounding ingredients, e.g. plasticisers, dyestuffs, fillers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F220/00Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
    • C08F220/02Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
    • C08F220/04Acids; Metal salts or ammonium salts thereof
    • C08F220/06Acrylic acid; Methacrylic acid; Metal salts or ammonium salts thereof
    • 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
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/139Processes of manufacture
    • 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
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • 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
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/621Binders
    • 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

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Abstract

PROBLEM TO BE SOLVED: To provide a method for preparing an aqueous binder for a lithium ion battery negative electrode having improved viscosity, low dispersion efficiency, and good cycle characteristics.SOLUTION: A method of preparing an aqueous binder for a lithium ion battery negative electrode is by the following procedure. A reactive emulsifier, a water-soluble acrylic monomer, an oil-soluble acrylic monomer, and an initiator solution are sequentially added and homogeneously mixed to obtain a base solution, the temperature is raised to initiate polymerization, and while maintaining stirring, a mixed solution of a water-soluble acrylic monomer and an oil-soluble acrylic monomer and an initiator solution are added and reacted.SELECTED DRAWING: Figure 4

Description

本発明はリチウムイオン電池技術の分野に属し、具体的には、リチウムイオン電池負極用水性バインダー及びその調製方法に関する。   The present invention belongs to the field of lithium ion battery technology, and specifically relates to an aqueous binder for a lithium ion battery negative electrode and a method for preparing the same.

新エネルギー事業は、新興産業として、省エネ・排出削減及び持続的な発展に関する国の方針と政策に従い、産業構造の調整及び転換に対して大いに助けになっている。リチウムイオン二次電池は、新エネルギー産業の中の非常に重要な構成部分として、現在、この業界において特に重要である。   The new energy business, as an emerging industry, has greatly helped to adjust and transform the industrial structure in accordance with national policies and policies on energy conservation, emission reduction and sustainable development. Lithium ion secondary batteries are currently of particular importance in this industry as a very important component in the new energy industry.

科学技術の発展及び人々の物質的・文化的生活の向上に伴い、リチウムイオン電池に対する人々の要求はますます高くなっている。リチウムイオン二次電池は、携帯電話などの3C製品、電気自動車、及び自動車に幅広く使用されており、その容量と使用寿命は、その大規模な普及及び用途に対して決定的に重要である。   With the development of science and technology and the improvement of people's material and cultural life, people's demands for lithium-ion batteries are increasing. Lithium ion secondary batteries are widely used in 3C products such as mobile phones, electric vehicles, and automobiles, and their capacity and service life are critical for their large-scale spread and use.

リチウムイオン電池は、通常、活物質、導電性添加剤及びバインダー溶液を混合しスラリー中に均一に粉砕し、電極片としての銅箔や、アルミニウム箔上に塗布し、乾燥、圧延及び他のプロセスによって処理してなるものである。リチウムイオン二次電池の容量と寿命は、電池電極片中の活物質の量、及び活物質と電極片を結着するためのバインダーの性能に依存する。活物質の量が多いほど、電池の容量が大きくなることを意味するが、電池製造中の活物質が多いほど、結着強度への影響が大きくなる。さらに、現在多く使用されるバインダーは含フッ素重合体バインダーであり、製造中に揮発するその溶剤は環境を汚染するだけでなく、作業者の健康に危害を及ぼす。また、含フッ素重合体の溶剤の価格は高いため、電池の製造コストを高騰させる。従って、安全かつ無公害で効率的な水性バインダーを開発してリチウムイオン電池に用いることは非常に重要な意義を有する。   Lithium ion batteries are usually mixed with an active material, conductive additive and binder solution, and uniformly pulverized in a slurry, applied on a copper foil or aluminum foil as an electrode piece, dried, rolled and other processes Is processed. The capacity and life of the lithium ion secondary battery depend on the amount of the active material in the battery electrode piece and the performance of the binder for binding the active material and the electrode piece. This means that the larger the amount of the active material, the larger the capacity of the battery. However, the more active material during battery manufacture, the greater the influence on the binding strength. In addition, the currently widely used binder is a fluoropolymer binder, and the solvent that volatilizes during production not only pollutes the environment but also poses a health hazard to workers. Moreover, since the price of the solvent for the fluoropolymer is high, the manufacturing cost of the battery is increased. Therefore, it is very important to develop a safe, pollution-free and efficient aqueous binder for use in lithium ion batteries.

リチウムイオン電池用バインダーは、主に、二種類に分けられる。一種類は油性バインダーであり、有機溶剤を分散剤として使用する。他の種類は水性バインダーであり、水を分散剤として使用する。油性バインダーと比較して、水性バインダーは、水を分散剤として使用するため、製造中に溶剤を放出せずに、環境に優しく、製造コストが低く、安全性が高いなどの利点を有し、バインダー産業の重要な発展方向となっている。現在、リチウムイオン電池負極の電極片用水性バインダーの調製においては、特許CN201310322571.2に記載されているように、カルボキシセルロースナトリウム(CMC)とスチレン-ブタジエンラテックス(SBR)を配合する手段が一般的に使用されている。この手段の欠点は、CMCを十分に溶解した後に負極関連材料及びSBRと混合し分散する必要があることである。しかしながら、水中でのCMCの溶解プロセスが遅く、非効率的であり、透明な粒子を生成し易く、分散性能が悪く、電池電極片の一致性に影響を与える。   Lithium ion battery binders are mainly divided into two types. One type is an oil-based binder, which uses an organic solvent as a dispersant. Another type is an aqueous binder, which uses water as a dispersant. Compared to oil-based binders, water-based binders use water as a dispersant, so they do not release solvents during production, have the advantages of being environmentally friendly, low in manufacturing costs, and high in safety. It is an important development direction of the binder industry. At present, in preparation of an aqueous binder for an electrode piece of a lithium ion battery negative electrode, as described in Patent CN201310322571.2, a means of blending sodium carboxycellulose (CMC) and styrene-butadiene latex (SBR) is generally used. Is used. The disadvantage of this measure is that the CMC needs to be sufficiently dissolved before it is mixed and dispersed with the negative electrode related material and SBR. However, the dissolution process of CMC in water is slow, inefficient, easy to produce transparent particles, poor dispersion performance, and affects the consistency of battery electrode pieces.

特許CN01108511.8には、リチウムイオン二次電池電極材料と集電体との水性バインダーの調製方法が開示されている。その技術的手段は次のとおりである。一般式CH=CRを有する親水性モノマーと親油性モノマーを初期重合ユニットとする。まず、1種、2種またはそれ以上の親水性モノマー及び1種、2種またはそれ以上の親油性モノマーを混合し、乳化剤および他の添加剤を添加する。過硫酸アンモニウムなどの水溶性開始剤、並びにそれがNaSO及びFeSOなどと構成したレドックス系を開始系として、30〜80℃の温度で、反応を3〜24時間行って、水性バインダーを得る。得られるバインダー共重合体の含有量が少なく、粘度が高く、分散効率に影響を与え、使用する試薬の種類が多く、反応時間が長くなり、水性バインダーの製造コストが高くなる。 Patent CN01108511.8 discloses a method for preparing an aqueous binder of a lithium ion secondary battery electrode material and a current collector. The technical means are as follows. A hydrophilic monomer and a lipophilic monomer having the general formula CH 2 = CR 1 R 2 are used as an initial polymerization unit. First, one, two or more hydrophilic monomers and one, two or more lipophilic monomers are mixed and an emulsifier and other additives are added. A water-soluble initiator such as ammonium persulfate and a redox system composed of NaSO 3 and FeSO 4 are used as an initiation system, and the reaction is performed at a temperature of 30 to 80 ° C. for 3 to 24 hours to obtain an aqueous binder. The resulting binder copolymer content is low, the viscosity is high, the dispersion efficiency is affected, the number of reagents used is large, the reaction time is long, and the production cost of the aqueous binder is high.

従来技術の欠陥を克服する。   Overcoming the deficiencies of the prior art.

本発明はリチウムイオン電池負極用水性バインダーの調製方法を提供し、その具体的な手順は以下のとおりである。
反応性乳化剤、水溶性アクリル系モノマー、油溶性アクリル系モノマー及び開始剤溶液を順に添加し均一混合してからベース液とし、昇温して重合を開始させ、迅速な撹拌を維持しながら、水溶性アクリル系モノマーと油溶性アクリル系モノマーの混合液及び開始剤溶液を添加し、高温で反応させて、リチウムイオン電池負極用水性バインダー溶液を調製する。
This invention provides the preparation method of the aqueous binder for lithium ion battery negative electrodes, The specific procedure is as follows.
Reactive emulsifier, water-soluble acrylic monomer, oil-soluble acrylic monomer and initiator solution are added in order and mixed uniformly, then used as a base solution, heated to start polymerization and maintain rapid stirring while maintaining water A mixed liquid of an acrylic acrylic monomer and an oil-soluble acrylic monomer and an initiator solution are added and reacted at a high temperature to prepare an aqueous binder solution for a lithium ion battery negative electrode.

前記ベース液における反応性乳化剤、水溶性アクリル系モノマー、油溶性アクリル系モノマー及び開始剤の割合は、重量で0.5〜3:20〜45:15〜80:0.1〜10であり、好ましくは1.0〜2.5:25〜40:25〜70:1.0〜8.0であり、さらに好ましくは1.5:25:60:0.5である。
前記ベース液の使用量は、総重量に対して10〜50%(重量%、以下同じ)を占め、好ましくは20〜40%である。
前記ベース液は、水を分散媒質とする。上記総重量は、ベース液の使用量、並びに滴下工程で反応系に添加されたモノマー混合液の使用量及び開始剤の使用量を含むが、水の使用量を含まない。
The ratio of the reactive emulsifier, the water-soluble acrylic monomer, the oil-soluble acrylic monomer and the initiator in the base liquid is 0.5 to 3:20 to 45:15 to 80: 0.1 to 10 by weight, Preferably it is 1.0-2.5: 25-40: 25-70: 1.0-8.0, More preferably, it is 1.5: 25: 60: 0.5.
The amount of the base solution used is 10 to 50% (% by weight, hereinafter the same) with respect to the total weight, and preferably 20 to 40%.
The base liquid uses water as a dispersion medium. The total weight includes the amount of the base solution used, the amount of the monomer mixture added to the reaction system in the dropping step, and the amount of initiator used, but does not include the amount of water used.

前記調製方法では、使用される水溶性アクリル系モノマーと油溶性アクリル系モノマーの割合は5〜40:20〜80であり、好ましくは20〜40:30〜60であり、さらに好ましくは25:36である。
前記開始剤溶液の使用量はアクリル系モノマーの総使用量の0.5〜6%を占め、前記アクリル系モノマーは水溶性アクリル系モノマーと油溶性アクリル系モノマーを含む。
前記リチウムイオン水性バインダーの固形分は30〜60%であり、好ましくは35〜55%である。
前記モノマー混合液の滴下時間は1〜3時間であり、好ましくは1.5〜2.5時間である。
前記モノマー混合液を2〜10分間滴下してから開始剤溶液の滴加を開始する。好ましくは5分間である。
前記反応温度は60〜90℃であり、好ましくは70〜85℃である。
前記反応時間は2〜6時間であり、好ましくは3〜5時間である。前記反応時間は、反応系内に開始剤を添加して重合反応を開始させてから計算する。
In the said preparation method, the ratio of the water-soluble acrylic monomer and oil-soluble acrylic monomer to be used is 5-40: 20-80, Preferably it is 20-40: 30-60, More preferably, it is 25:36 It is.
The amount of the initiator solution used accounts for 0.5 to 6% of the total amount of acrylic monomer used, and the acrylic monomer includes a water-soluble acrylic monomer and an oil-soluble acrylic monomer.
The lithium ion aqueous binder has a solid content of 30 to 60%, preferably 35 to 55%.
The dropping time of the monomer mixture is 1 to 3 hours, preferably 1.5 to 2.5 hours.
The monomer mixture is added dropwise for 2-10 minutes and then the initiator solution is added dropwise. Preferably it is 5 minutes.
The said reaction temperature is 60-90 degreeC, Preferably it is 70-85 degreeC.
The reaction time is 2 to 6 hours, preferably 3 to 5 hours. The reaction time is calculated after an initiator is added to the reaction system to initiate the polymerization reaction.

前記反応性乳化剤は、親水基、親油基及び1つ以上の反応性基を同時に含む化合物である。前記反応性基は、重合反応に関与する基、例えば、炭素-炭素二重結合、炭素-炭素三重結合、カルボニルなどの不飽和結合、−OH、−COOH、−NHなどである。
好ましくは、前記反応性乳化剤は、アクリルアミドイソプロピルスルホン酸ナトリウム、ビニルスルホン酸ナトリウム、2−アリルエーテル−3−ヒドロキシプロパン−1−スルホン酸ナトリウム、アリルエーテルヒドロキシプロパンスルホン酸ナトリウムなどの中の1種以上から選択される。
The reactive emulsifier is a compound that simultaneously contains a hydrophilic group, a lipophilic group and one or more reactive groups. The reactive group is a group involved in a polymerization reaction, for example, a carbon-carbon double bond, a carbon-carbon triple bond, an unsaturated bond such as carbonyl, —OH, —COOH, —NH 2 or the like.
Preferably, the reactive emulsifier is one or more of sodium acrylamide isopropyl sulfonate, sodium vinyl sulfonate, sodium 2-allyl ether-3-hydroxypropane-1-sulfonate, sodium allyl ether hydroxypropane sulfonate, and the like. Selected from.

前記水溶性アクリル系モノマーは、一般式CH=CRを有し、ここで、R=H、−CH、−COOH、R=−COOH、−CN、−CONH、−COONa、−CHCOOH、−OOCCH、−COOCHCHOH、−COOCHCHCHOHである。
好ましくは、前記水溶性アクリル系モノマーは、アクリル酸、メタクリル酸、アクリロニトリル、アクリルアミド、アクリル酸ナトリウム、イタコン酸、N−ヒドロキシメチルアクリルアミド、ヒドロキシエチルアクリレート及びヒドロキシプロピルアクリレートの中の1種以上から選択される。
The water-soluble acrylic monomer has the general formula CH 2 = CR 1 R 2, wherein, R 1 = H, -CH 3 , -COOH, R 2 = -COOH, -CN, -CONH 2, - COONa, -CH 2 COOH, -OOCCH 3 , -COOCH 2 CH 2 OH, a -COOCH 2 CH 2 CH 2 OH.
Preferably, the water-soluble acrylic monomer is selected from one or more of acrylic acid, methacrylic acid, acrylonitrile, acrylamide, sodium acrylate, itaconic acid, N-hydroxymethyl acrylamide, hydroxyethyl acrylate and hydroxypropyl acrylate. The

前記油溶性アクリル系モノマーは、一般式CH=CRを有し、ここで、R=H、−CH、−COOH、R=−COOCH、−COOCHCH、−COO(CHCH、−COOCHCH(CHCH)CHCHCHCH、−COO(CH11CH
である。
好ましくは、前記油溶性アクリル系モノマーは、アクリル酸メチル、メタクリル酸メチル、アクリル酸エチル、アクリル酸プロピル、アクリル酸ブチル、アクリル酸オクチル、アクリル酸ラウリル、及びアクリル酸イソボルニルの中の1種以上から選択される。
The oil-soluble acrylic monomer has the general formula CH 2 = CR 3 R 4, wherein, R 3 = H, -CH 3 , -COOH, R 4 = -COOCH 3, -COOCH 2 CH 3, - COO (CH 2) 2 CH 3 , -COOCH 2 CH (CH 2 CH 3) CH 2 CH 2 CH 2 CH 3, -COO (CH 2) 11 CH 3,
It is.
Preferably, the oil-soluble acrylic monomer is one or more of methyl acrylate, methyl methacrylate, ethyl acrylate, propyl acrylate, butyl acrylate, octyl acrylate, lauryl acrylate, and isobornyl acrylate. Selected.

前記開始剤は、過硫酸カリウム、過硫酸アンモニウム、過硫酸ナトリウム、亜硫酸ナトリウム、亜硫酸水素ナトリウム、2,2’−アゾビス(2,4−ジメチルバレロニトリル)及びアゾビスイソブチロニトリルの中の1種以上から選択される。   The initiator is one of potassium persulfate, ammonium persulfate, sodium persulfate, sodium sulfite, sodium hydrogen sulfite, 2,2′-azobis (2,4-dimethylvaleronitrile) and azobisisobutyronitrile. Selected from the above.

前記開始剤溶液は上記開始剤の水溶液であり、その質量百分率は5〜20%である。
前記リチウムイオン電池負極用水性バインダーの調製は、200〜800rpmの高速撹拌で行われ、反応中に窒素ガスによる保護状態が維持される。
本発明の1つの実施例において、前記リチウムイオン電池負極用水性バインダーの調製方法は、その具体的な手順が以下のとおりである。
反応性乳化剤、水溶性アクリル系モノマー、油溶性アクリル系モノマーを順に添加し、200〜800rpmで均一に撹拌し、窒素ガスを供給する。反応系の温度は70〜80℃である。開始剤を添加して均一混合した後、ベース液とする。ベース液中の反応性乳化剤、水溶性アクリル系モノマー、油溶性アクリル系モノマー及び開始剤の割合は、重量で、1.5:25:60:0.5であり、ベース液の使用量は総重量の20〜40%を占める。0.5〜1.5時間の反応後に、撹拌しながら水溶性と油溶性アクリル系モノマーの混合液を滴下し、モノマー混合液を2〜10分間滴下してから開始剤溶液の滴下を開始し、滴下時間は1.5〜2.5時間である。滴下完了後に反応系の温度を70〜85℃に上昇させ且つ0.5〜1.5時間保温して、リチウムイオン電池負極用水性バインダーを得る。調製過程全体に亘って使用された水溶性アクリル系モノマーと油溶性アクリル系モノマーの割合は25:36であり、リチウムイオン水性バインダーの固形分は35〜55%である。
The initiator solution is an aqueous solution of the initiator, and the mass percentage is 5 to 20%.
The aqueous binder for a lithium ion battery negative electrode is prepared by high-speed stirring at 200 to 800 rpm, and a protected state by nitrogen gas is maintained during the reaction.
In one embodiment of the present invention, the specific procedure for preparing the aqueous binder for a lithium ion battery negative electrode is as follows.
A reactive emulsifier, a water-soluble acrylic monomer, and an oil-soluble acrylic monomer are added in order, and the mixture is stirred uniformly at 200 to 800 rpm, and nitrogen gas is supplied. The temperature of the reaction system is 70-80 ° C. After adding an initiator and mixing uniformly, it is set as a base liquid. The ratio of reactive emulsifier, water-soluble acrylic monomer, oil-soluble acrylic monomer and initiator in the base solution is 1.5: 25: 60: 0.5 by weight, and the amount of base solution used is the total It accounts for 20-40% of the weight. After the reaction for 0.5 to 1.5 hours, a mixture of water-soluble and oil-soluble acrylic monomer is added dropwise with stirring, the monomer mixture is added dropwise for 2 to 10 minutes, and then the initiator solution is added dropwise. The dropping time is 1.5 to 2.5 hours. After completion of the dropwise addition, the temperature of the reaction system is raised to 70 to 85 ° C. and kept for 0.5 to 1.5 hours to obtain an aqueous binder for a lithium ion battery negative electrode. The ratio of water-soluble acrylic monomer to oil-soluble acrylic monomer used throughout the preparation process is 25:36, and the solid content of the lithium ion aqueous binder is 35-55%.

本発明の他の態様は、リチウムイオン電池負極用水性バインダーを提供する。該リチウムイオン電池負極用水性バインダーは上記調製方法により得られ、外観が乳液状の粘性液体である。その固形分の範囲は30〜60%であり、好ましくは35〜55%である。その粘度範囲は500〜8000mPa・sであり、好ましくは500〜5000mPa・sである。
本発明のリチウムイオン電池負極用水性バインダーに適する電極材料はコークス、天然黒鉛、人造黒鉛、LiCoO、LiNiO、LiMn、LiFePO、Ni、Co、Mn三元系複合酸化物などである。
Another aspect of the present invention provides an aqueous binder for a lithium ion battery negative electrode. The aqueous binder for a lithium ion battery negative electrode is obtained by the above preparation method, and is a viscous liquid whose appearance is emulsion. The range of the solid content is 30 to 60%, preferably 35 to 55%. The viscosity range is 500 to 8000 mPa · s, preferably 500 to 5000 mPa · s.
Suitable electrode materials for the aqueous binder for lithium ion battery negative electrode of the present invention include coke, natural graphite, artificial graphite, LiCoO 2 , LiNiO 2 , LiMn 2 O 4 , LiFePO 4 , Ni, Co, Mn ternary composite oxide, etc. is there.

本発明の他の態様は、リチウムイオン電池の電極片を提供する。該電極片は、上記水性バインダーと電極活性材料を用い混合してスラリーを調製し、集電材上に塗布し乾燥してなるものである。前記スラリーにおける水性バインダーの含有量は1〜8%であり、好ましくは2〜6%である。
本発明の他の態様は、リチウムイオン電池を提供する。該リチウムイオン電池は、正極、負極、電解液、分離膜を備え、正極及び/又は負極は上記のリチウムイオン電池の電極片である。
Another aspect of the present invention provides an electrode piece for a lithium ion battery. The electrode piece is prepared by mixing the aqueous binder and the electrode active material to prepare a slurry, which is applied onto a current collector and dried. The content of the aqueous binder in the slurry is 1 to 8%, preferably 2 to 6%.
Another aspect of the present invention provides a lithium ion battery. The lithium ion battery includes a positive electrode, a negative electrode, an electrolytic solution, and a separation membrane, and the positive electrode and / or the negative electrode are electrode pieces of the above-described lithium ion battery.

本発明によるリチウムイオン電池負極用水性バインダーの調製方法は、操作工程が簡単であり、反応時間が短く、反応が十分である。調製されたリチウムイオン電池負極用水性バインダーは乳液状の粘性液体であり、固形分が高く、結着性能が優れた特徴を有し、機械的安定性が良好であるため、分散プロセスにおいて凝集や他の解乳化現象が生じない。表面張力が小さく、導電剤と電極材料の分散が更に容易になされ、分散効率及びフィルム形成性が大きく向上する。同時に、この方法により調製されたバインダーは良好な柔軟性及び良好な流動性を有し、形成されたフィルムは柔らかく、製造された電池電極片はスムーズであり、一致性が良い。この電極片を用いて製造された電池のサイクル性能は良好であり、0.5cでサイクルを450回行った後の電池容量維持率は90%以上である。   The method for preparing an aqueous binder for a lithium ion battery negative electrode according to the present invention has a simple operation process, a short reaction time, and a sufficient reaction. The prepared aqueous binder for lithium ion battery negative electrode is an emulsion viscous liquid, has a high solid content, excellent binding performance, and good mechanical stability. No other demulsification phenomenon occurs. The surface tension is low, the conductive agent and the electrode material are more easily dispersed, and the dispersion efficiency and film formability are greatly improved. At the same time, the binder prepared by this method has good flexibility and good fluidity, the formed film is soft, the produced battery electrode pieces are smooth and have good consistency. The battery manufactured using this electrode piece has good cycle performance, and the battery capacity retention rate after 450 cycles at 0.5c is 90% or more.

本発明の実施例4によるリチウムイオン電池負極用水性バインダーのTG−DSC曲線である。It is a TG-DSC curve of the aqueous binder for lithium ion battery negative electrodes by Example 4 of this invention. 実施例5による試験用リチウムイオン電池の充放電曲線である。実施例2で調製した水性バインダーを用いて負極電極片を製造し、正極電極片と組み合わせて上記リチウムイオン電池を得る。ここで、縦軸は電池電圧(V)、横軸は容量(mAh)である。1は充電曲線であり、2は放電曲線である。6 is a charge / discharge curve of a test lithium ion battery according to Example 5. FIG. A negative electrode piece is produced using the aqueous binder prepared in Example 2, and the lithium ion battery is obtained in combination with the positive electrode piece. Here, the vertical axis represents battery voltage (V), and the horizontal axis represents capacity (mAh). 1 is a charge curve and 2 is a discharge curve. 実施例5による試験用リチウムイオン電池のサイクリックボルタモグラムであり、実施例2で調製した水性バインダーを用いて負極電極片を製造し、金属リチウムの正極電極片と組み合わせて上記リチウムイオン電池を得る。ここで、縦軸は電流(mA)、横軸は電位(v)である。It is a cyclic voltammogram of the test lithium ion battery by Example 5, a negative electrode piece is manufactured using the aqueous binder prepared in Example 2, and it combines with the positive electrode piece of metallic lithium, and obtains the said lithium ion battery. Here, the vertical axis represents current (mA), and the horizontal axis represents potential (v). 実施例5による試験用リチウムイオン電池の充放電サイクルグラフである。実施例2で調製した水性バインダーを用いて負極電極片を製造し、正極電極片と組み合わせて上記リチウムイオン電池を得る。ここで、縦軸は容量維持率であり、横軸は充放電サイクルの回数(回)である。6 is a charge / discharge cycle graph of a test lithium ion battery according to Example 5. FIG. A negative electrode piece is produced using the aqueous binder prepared in Example 2, and the lithium ion battery is obtained in combination with the positive electrode piece. Here, the vertical axis represents the capacity maintenance rate, and the horizontal axis represents the number of times of charging / discharging cycles (times).

以下、本発明の実施形態に係る添付図面を参照しながら、本発明の実施形態に係る技術的解決手段を明確かつ詳細に説明する。当然のことながら、ここで説明する実施形態は本発明の諸実施形態の全てではなく一部にすぎない。当業者が創造的な作業なしに本発明の諸実施形態に基づいて得られる他の全ての実施形態は、本発明の保護範囲に含まれるべきである。
〈実施例1〉
DESCRIPTION OF EMBODIMENTS Hereinafter, technical solutions according to embodiments of the present invention will be described clearly and in detail with reference to the accompanying drawings according to embodiments of the present invention. Of course, the embodiments described herein are only a part rather than all of the embodiments of the present invention. All other embodiments obtained by a person of ordinary skill in the art based on the embodiments of the present invention without creative efforts shall fall within the protection scope of the present invention.
<Example 1>

本実施例では、ビニルスルホン酸ナトリウム、アクリル酸及びアクリル酸エチルはそれぞれ反応性乳化剤、親水性アクリル系モノマー及び親油性アクリル系モノマーとして使用され、調製過程全体において三者の割合は0.5:25:60であった。   In this example, sodium vinyl sulfonate, acrylic acid and ethyl acrylate are used as reactive emulsifier, hydrophilic acrylic monomer and lipophilic acrylic monomer, respectively, and the ratio of the three in the whole preparation process is 0.5: It was 25:60.

以下の手順に従って、リチウムイオン電池負極用水性バインダーの乳化液を調製した。反応釜中に、1.5部のビニルスルホン酸ナトリウム、25部のアクリル酸、60部のアクリル酸エチル、及び水を順に添加し混合攪拌した。回転速度は200rpmであった。窒素ガスを供給し、72℃で温度を一定に維持し、0.5部の10%過硫酸アンモニウム水溶液を添加し、重合を開始させた。反応時間は50分であった。そして、50部のアクリル酸、120部のアクリル酸エチル水溶液及び10部の10%(質量百分率)過硫酸アンモニウム水溶液をゆっくりと滴下した。滴下時間は3時間であり、滴下時の反応系の温度は75℃であった。滴下終了後に、温度を80℃に上昇して60分保温して、リチウムイオン電池用水性バインダーの乳化液を得た。   An emulsion of an aqueous binder for a lithium ion battery negative electrode was prepared according to the following procedure. In the reaction kettle, 1.5 parts of sodium vinyl sulfonate, 25 parts of acrylic acid, 60 parts of ethyl acrylate, and water were added in order and mixed and stirred. The rotation speed was 200 rpm. Nitrogen gas was supplied, the temperature was kept constant at 72 ° C., and 0.5 part of 10% aqueous ammonium persulfate solution was added to initiate the polymerization. The reaction time was 50 minutes. Then 50 parts of acrylic acid, 120 parts of ethyl acrylate aqueous solution and 10 parts of 10% (percent by mass) ammonium persulfate aqueous solution were slowly added dropwise. The dropping time was 3 hours, and the temperature of the reaction system at the time of dropping was 75 ° C. After completion of the dropping, the temperature was raised to 80 ° C. and kept for 60 minutes to obtain an emulsion of an aqueous binder for lithium ion batteries.

調製された水性バインダーは乳白色の粘性液体であり、その固形分は40%、粘度は800mPa・sであった。
〈実施例2〉
The prepared aqueous binder was a milky white viscous liquid having a solid content of 40% and a viscosity of 800 mPa · s.
<Example 2>

本実施例では、反応釜に順に添加した成分及びその割合は、1.5部のビニルスルホン酸ナトリウム、12.5部のアクリル酸、30部のアクリル酸エチル、及び水であった。滴下した成分及びその割合は、62.5部のアクリル酸、及び150部のアクリル酸エチルであった。他のステップは実施例1と同じであった。
調製された水性バインダーは乳液状の粘性液体であり、その固形分は40%であり、粘度は1000〜1500mPa・sであった。
〈実施例3〉
In this example, the components and proportions added sequentially to the reaction kettle were 1.5 parts sodium vinyl sulfonate, 12.5 parts acrylic acid, 30 parts ethyl acrylate, and water. The components dropped and their proportions were 62.5 parts acrylic acid and 150 parts ethyl acrylate. The other steps were the same as in Example 1.
The prepared aqueous binder was an emulsion viscous liquid, the solid content was 40%, and the viscosity was 1000-1500 mPa · s.
<Example 3>

本実施例では、水溶性アクリル系モノマーと油溶性アクリル系モノマーはそれぞれヒドロキシエチルアクリレートとアクリル酸ブチルであり、他のステップは実施例1と同じであった。   In this example, the water-soluble acrylic monomer and the oil-soluble acrylic monomer were hydroxyethyl acrylate and butyl acrylate, respectively, and the other steps were the same as in Example 1.

調製された水性バインダーは乳液状の粘性液体であり、その固形分は50%、粘度は1500mPa・sであった。
〈実施例4〉
The prepared aqueous binder was an emulsion viscous liquid, the solid content was 50%, and the viscosity was 1500 mPa · s.
<Example 4>

本実施例では、アリルエーテルヒドロキシプロパンスルホン酸ナトリウム、アクリルアミド、アクリル酸ラウリル及びアゾビスイソブチロニトリルをそれぞれ反応性乳化剤、親水性アクリル系モノマー、親油性アクリル系モノマー及び開始剤として用いた。ベース液における反応性乳化剤、水溶性アクリル系モノマー、油溶性アクリル系モノマー及び開始剤の割合は0.6:20:80:10であり、ベース液は総重量の30%を占め、他のステップは実施例1と同じであった。   In this example, sodium allyl ether hydroxypropane sulfonate, acrylamide, lauryl acrylate, and azobisisobutyronitrile were used as a reactive emulsifier, a hydrophilic acrylic monomer, a lipophilic acrylic monomer, and an initiator, respectively. The ratio of reactive emulsifier, water-soluble acrylic monomer, oil-soluble acrylic monomer and initiator in the base solution is 0.6: 20: 80: 10, the base solution accounts for 30% of the total weight, and other steps Was the same as in Example 1.

調製された水性バインダーは乳液状の粘性液体であり、その固形分は40%であり、粘度は1000mPa・sであり、機械的安定性が良好であり、分散プロセスにおいて5000rpmで分散され、安定的に存在することができる。   The prepared aqueous binder is an emulsion viscous liquid, the solid content is 40%, the viscosity is 1000 mPa · s, the mechanical stability is good, and the dispersion process is stable at 5000 rpm. Can exist.

上記水性バインダーのTG−DSC曲線を図1に示す。曲線から、該水性バインダーは熱安定性に優れ、分解温度は270℃より高いことが分かった。
〈実施例5〉
The TG-DSC curve of the aqueous binder is shown in FIG. From the curve, it was found that the aqueous binder was excellent in thermal stability and the decomposition temperature was higher than 270 ° C.
<Example 5>

BTR518人造黒鉛を負極材料として、実施例2で合成した水性バインダーの乳化液を用いて、負極スラリーを調整した。負極スラリー全体における材料の割合は、水性バインダーが3.5%、BTR518人造黒鉛が95.5%、導電剤S−Pが1%であった。   A negative electrode slurry was prepared using the emulsion of the aqueous binder synthesized in Example 2 using BTR518 artificial graphite as a negative electrode material. The ratio of the material in the whole negative electrode slurry was 3.5% for the aqueous binder, 95.5% for the BTR518 artificial graphite, and 1% for the conductive agent SP.

上記の調製された負極スラリーの固形分は58%であり、粘度は3000mPa・sであった。このスラリーからなる負極電極片は滑らかであり、一致性が良好であり、面密度が高い。   The prepared negative electrode slurry had a solid content of 58% and a viscosity of 3000 mPa · s. The negative electrode piece made of this slurry is smooth, has good consistency, and has a high surface density.

上記の負極電極片をマンガン酸リチウム(BN−M01)活物質と組み合わせて試験用リチウムイオン電池を製造し、応用試験を行った。結果を図2〜4に示す。図2は、上記の試験用リチウムイオン電池の充放電曲線である。図2に示すように、試験電池の充放電終止電圧は3.10〜4.20Vであった。図3は、上記の試験用リチウムイオン電池のサイクリックボルタモグラムである。図4は、上記の試験用リチウムイオン電池の充放電サイクルグラフである。図4に示すように、試験電池の初回の充放電容量は96%より大きく、容量の発揮に優れ、放電曲線の平坦域は安定であった。0.5cでサイクルを200回行った後でも、電池容量維持率は明らかに低下せず、基本的に97.0%以上に維持された。0.5cでサイクルを450回行った後に、電池容量維持率は90%以上であり、容量の減衰は小さかった。
〈実施例6〉
A lithium ion battery for test was manufactured by combining the above negative electrode piece with a lithium manganate (BN-M01) active material, and an application test was performed. The results are shown in FIGS. FIG. 2 is a charge / discharge curve of the test lithium ion battery. As shown in FIG. 2, the charge / discharge end voltage of the test battery was 3.10 to 4.20V. FIG. 3 is a cyclic voltammogram of the above-described test lithium ion battery. FIG. 4 is a charge / discharge cycle graph of the above-described test lithium ion battery. As shown in FIG. 4, the initial charge / discharge capacity of the test battery was larger than 96%, the capacity was excellent, and the flat region of the discharge curve was stable. Even after 200 cycles at 0.5c, the battery capacity retention rate was not clearly reduced and was basically maintained at 97.0% or more. After performing the cycle 450 times at 0.5c, the battery capacity retention rate was 90% or more, and the capacity decay was small.
<Example 6>

黒鉛Q10を負極材料として、実施例2で合成した水性バインダーの乳化液を用いて、負極スラリーを調製した。負極スラリー全体における材料の割合は、水性バインダーが3.5%、黒鉛Q10が95.5%、導電剤S−Pが1%である。   A negative electrode slurry was prepared using the emulsion of the aqueous binder synthesized in Example 2 using graphite Q10 as the negative electrode material. The ratio of the material in the whole negative electrode slurry is 3.5% for the aqueous binder, 95.5% for the graphite Q10, and 1% for the conductive agent SP.

上記の調製された負極スラリーの固形分は48%であり、スラリーの粘度は3400センチポアズであった。このスラリーからなる負極電極片は滑らかであり、一致性が良好である。   The solid content of the prepared negative electrode slurry was 48%, and the viscosity of the slurry was 3400 centipoise. The negative electrode piece made of this slurry is smooth and has good consistency.

上記負極電極片をマンガン酸リチウム(BN−M01)活物質と組み合わせて、2つの試験用リチウムイオン電池を製造し、それぞれに電池1と電池2の番号を付けた。電池のサイクル性能検出及び落下試験を行った。結果を表1〜2に示す。   Two lithium ion batteries for test were manufactured by combining the negative electrode piece with a lithium manganate (BN-M01) active material, and the numbers of the battery 1 and the battery 2 were given to the batteries. Battery cycle performance detection and drop test were performed. The results are shown in Tables 1-2.

表1 サイクル性能検出結果

Table 1 Results of cycle performance detection

電池1と電池2は、0.5Cでサイクルを20回行った容量/初期容量がそれぞれ99.6%と99.7%(標準≧96%)であり、1Cでサイクルを20回行った容量/初期容量がそれぞれ99.2%と99.2%(標準≧95%)であり、基準を満たす。   Battery 1 and Battery 2 have capacity of 99.6% and 99.7% (standard ≧ 96%) after 20 cycles at 0.5 C, respectively, and capacity after 20 cycles at 1 C. / The initial capacities are 99.2% and 99.2% (standard ≧ 95%), respectively, which meet the criteria.

表2 落下試験結果

Table 2 Drop test results

測定結果は以下のとおりである。電池は、発煙、発火、爆発及び液漏れが生じなかった。常温で、1Cの電流で充電/放電サイクルを3回行った後の電池1と電池2の容量維持率はいずれも95%以上であり、即ちその容量維持率はいずれも85%より大きかった。   The measurement results are as follows. The battery did not smoke, ignite, explode or leak. The battery 1 and the battery 2 each had a capacity retention rate of 95% or more after the charge / discharge cycle was performed three times at a current of 1 C at room temperature, that is, the capacity retention rates were both greater than 85%.

上記は本発明の好適な実施形態に過ぎず、本発明はこれに限定されるものでなく、本発明の精神および原則内に属する限り、行われるすべての修正、同等の置き換えなどは、いずれも本発明の保護範囲内に含まれるべきである。   The above is only a preferred embodiment of the present invention, and the present invention is not limited to this, and all modifications, equivalent replacements, etc. made within the spirit and principle of the present invention are all included. It should be included within the protection scope of the present invention.

Claims (10)

リチウムイオン電池負極用水性バインダーの調製方法であって、
反応性乳化剤、水溶性アクリル系モノマー、油溶性アクリル系モノマー及び開始剤溶液を順に添加し均一混合してからベース液とし、昇温して重合を開始させ、撹拌を維持しながら、水溶性アクリル系モノマーと油溶性アクリル系モノマーの混合液及び開始剤溶液を添加し反応させて、リチウムイオン電池負極用水性バインダーを調製する、リチウムイオン電池負極用水性バインダーの調製方法。
A method for preparing an aqueous binder for a lithium ion battery negative electrode, comprising:
Reactive emulsifier, water-soluble acrylic monomer, oil-soluble acrylic monomer and initiator solution are added in order and mixed uniformly, then used as a base solution, polymerization is started by raising the temperature, and while maintaining stirring, water-soluble acrylic A method for preparing an aqueous binder for a lithium ion battery negative electrode, wherein a mixed liquid of an acrylic monomer and an oil-soluble acrylic monomer and an initiator solution are added and reacted to prepare an aqueous binder for a lithium ion battery negative electrode.
前記反応性乳化剤は、アクリルアミドイソプロピルスルホン酸ナトリウム、ビニルスルホン酸ナトリウム、2−アリルエーテル−3−ヒドロキシプロパン−1−スルホン酸ナトリウム、アリルエーテルヒドロキシプロパンスルホン酸ナトリウムの中の1種以上から選択される、請求項1に記載のリチウムイオン電池負極用水性バインダーの調製方法。   The reactive emulsifier is selected from one or more of sodium acrylamide isopropyl sulfonate, sodium vinyl sulfonate, sodium 2-allyl ether-3-hydroxypropane-1-sulfonate, and sodium allyl ether hydroxypropane sulfonate. The preparation method of the aqueous binder for lithium ion battery negative electrodes of Claim 1. 前記水溶性アクリル系モノマーは、一般式CH=CRを有し、ここで、R=H、−CH、−COOH、R=−COOH、−CN、−CONH、−COONa、−CHCOOH、−OOCCH、−COOCHCHOH、−COOCHCHCHOHであり、及び/又は、
前記油溶性アクリル系モノマーは、一般式CH=CRを有し、ここで、R=H、−CH、−COOH、R=−COOCH、−COOCHCH、−COO(CHCH、−COOCHCH(CHCH)CHCHCHCH、−COO(CH11CH
である、請求項1に記載のリチウムイオン電池負極用水性バインダーの調製方法。
The water-soluble acrylic monomer has the general formula CH 2 = CR 1 R 2, wherein, R 1 = H, -CH 3 , -COOH, R 2 = -COOH, -CN, -CONH 2, - COONa, -CH 2 COOH, -OOCCH 3 , -COOCH 2 CH 2 OH, a -COOCH 2 CH 2 CH 2 OH, and / or,
The oil-soluble acrylic monomer has the general formula CH 2 = CR 3 R 4, wherein, R 3 = H, -CH 3 , -COOH, R 4 = -COOCH 3, -COOCH 2 CH 3, - COO (CH 2) 2 CH 3 , -COOCH 2 CH (CH 2 CH 3) CH 2 CH 2 CH 2 CH 3, -COO (CH 2) 11 CH 3,
The method for preparing an aqueous binder for a lithium ion battery negative electrode according to claim 1, wherein
前記水溶性アクリル系モノマーは、アクリル酸、メタクリル酸、アクリロニトリル、アクリルアミド、アクリル酸ナトリウム、イタコン酸、N−ヒドロキシメチルアクリルアミド、ヒドロキシエチルアクリレート及びヒドロキシプロピルアクリレートの中の1種以上から選択され、及び/又は、
前記油溶性アクリル系モノマーは、アクリル酸メチル、メタクリル酸メチル、アクリル酸エチル、アクリル酸プロピル、アクリル酸ブチル、アクリル酸オクチル、アクリル酸ラウリル、及びアクリル酸イソボルニルの中の1種以上から選択される、請求項3に記載のリチウムイオン電池負極用水性バインダーの調製方法。
The water-soluble acrylic monomer is selected from one or more of acrylic acid, methacrylic acid, acrylonitrile, acrylamide, sodium acrylate, itaconic acid, N-hydroxymethyl acrylamide, hydroxyethyl acrylate and hydroxypropyl acrylate, and / or Or
The oil-soluble acrylic monomer is selected from one or more of methyl acrylate, methyl methacrylate, ethyl acrylate, propyl acrylate, butyl acrylate, octyl acrylate, lauryl acrylate, and isobornyl acrylate. The preparation method of the aqueous binder for lithium ion battery negative electrodes of Claim 3.
前記開始剤は、過硫酸カリウム、過硫酸アンモニウム、過硫酸ナトリウム、亜硫酸ナトリウム、亜硫酸水素ナトリウム、2,2’−アゾビス(2,4−ジメチルバレロニトリル)及びアゾビスイソブチロニトリルの中の1種以上から選択される、請求項1に記載のリチウムイオン電池負極用水性バインダーの調製方法。   The initiator is one of potassium persulfate, ammonium persulfate, sodium persulfate, sodium sulfite, sodium hydrogen sulfite, 2,2′-azobis (2,4-dimethylvaleronitrile) and azobisisobutyronitrile. The preparation method of the aqueous binder for lithium ion battery negative electrodes of Claim 1 selected from the above. 前記ベース液における反応性乳化剤、水溶性アクリル系モノマー、油溶性アクリル系モノマー及び開始剤の割合は、重量で0.5〜3:20〜45:15〜80:0.1〜10であり、前記ベース液の使用量は、総重量に対して10〜50%を占め、前記リチウムイオン電池負極用水性バインダーの固形分は30〜60%である、請求項1に記載のリチウムイオン電池負極用水性バインダーの調製方法。   The ratio of the reactive emulsifier, the water-soluble acrylic monomer, the oil-soluble acrylic monomer and the initiator in the base liquid is 0.5 to 3:20 to 45:15 to 80: 0.1 to 10 by weight, 2. The lithium ion battery negative electrode according to claim 1, wherein the amount of the base liquid used is 10 to 50% of the total weight, and the solid content of the lithium ion battery negative electrode aqueous binder is 30 to 60%. A method for preparing an aqueous binder. 前記調製方法では、使用される水溶性アクリル系モノマーと油溶性アクリル系モノマーの割合は5〜40:20〜80であり、及び/又は、前記モノマー混合液を2〜10分間滴下してから開始剤溶液の滴加を開始し、及び/又は、前記開始剤溶液の使用量は、アクリル系モノマーの総使用量の0.5〜6%を占める、請求項1に記載のリチウムイオン電池負極用水性バインダーの調製方法。   In the preparation method, the ratio of the water-soluble acrylic monomer to the oil-soluble acrylic monomer used is 5 to 40:20 to 80, and / or after the monomer mixture is dropped for 2 to 10 minutes. The lithium ion battery negative electrode according to claim 1, wherein the addition of the initiator solution is started and / or the usage amount of the initiator solution occupies 0.5 to 6% of the total usage amount of the acrylic monomer. A method for preparing an aqueous binder. 前記モノマー混合液の滴下時間は1〜3時間であり、及び/又は、反応温度は60〜90℃であり、及び/又は、反応時間は2〜6時間である、請求項1に記載のリチウムイオン電池負極用水性バインダーの調製方法。   2. The lithium according to claim 1, wherein a dropping time of the monomer mixture is 1 to 3 hours and / or a reaction temperature is 60 to 90 ° C. and / or a reaction time is 2 to 6 hours. A method for preparing an aqueous binder for an ion battery negative electrode. 前記リチウムイオン電池負極用水性バインダーの調製は200〜800rpmの攪拌で行われ、反応中に窒素ガスによる保護状態が維持される、請求項1に記載のリチウムイオン電池負極用水性バインダーの調製方法。   The method for preparing an aqueous binder for a lithium ion battery negative electrode according to claim 1, wherein the aqueous binder for a lithium ion battery negative electrode is prepared by stirring at 200 to 800 rpm, and the protection state by nitrogen gas is maintained during the reaction. リチウムイオン電池負極用水性バインダーであって、前記リチウムイオン電池負極用水性バインダーは、請求項1〜9のいずれか一項に記載のリチウムイオン電池負極用水性バインダーの調製方法により調製され、その固形分は30〜60%であり、粘度範囲は500〜8000mPa・sである、リチウムイオン電池負極用水性バインダー。   An aqueous binder for a lithium ion battery negative electrode, wherein the aqueous binder for a lithium ion battery negative electrode is prepared by the method for preparing an aqueous binder for a lithium ion battery negative electrode according to any one of claims 1 to 9, and is solid. An aqueous binder for a lithium ion battery negative electrode having a content of 30 to 60% and a viscosity range of 500 to 8000 mPa · s.
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