WO2016002586A1 - 蓄電デバイス用バインダー組成物 - Google Patents
蓄電デバイス用バインダー組成物 Download PDFInfo
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- WO2016002586A1 WO2016002586A1 PCT/JP2015/068030 JP2015068030W WO2016002586A1 WO 2016002586 A1 WO2016002586 A1 WO 2016002586A1 JP 2015068030 W JP2015068030 W JP 2015068030W WO 2016002586 A1 WO2016002586 A1 WO 2016002586A1
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
- H01M4/621—Binders
- H01M4/622—Binders being polymers
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
- H01M4/621—Binders
- H01M4/622—Binders being polymers
- H01M4/623—Binders being polymers fluorinated polymers
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D109/00—Coating compositions based on homopolymers or copolymers of conjugated diene hydrocarbons
- C09D109/06—Copolymers with styrene
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D133/00—Coating compositions based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Coating compositions based on derivatives of such polymers
- C09D133/04—Homopolymers or copolymers of esters
- C09D133/06—Homopolymers or copolymers of esters of esters containing only carbon, hydrogen and oxygen, the oxygen atom being present only as part of the carboxyl radical
- C09D133/10—Homopolymers or copolymers of methacrylic acid esters
- C09D133/12—Homopolymers or copolymers of methyl methacrylate
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D133/00—Coating compositions based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Coating compositions based on derivatives of such polymers
- C09D133/18—Homopolymers or copolymers of nitriles
- C09D133/20—Homopolymers or copolymers of acrylonitrile
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D151/00—Coating compositions based on graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Coating compositions based on derivatives of such polymers
- C09D151/06—Coating compositions based on graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Coating compositions based on derivatives of such polymers grafted on to homopolymers or copolymers of aliphatic hydrocarbons containing only one carbon-to-carbon double bond
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D5/00—Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes
- C09D5/24—Electrically-conducting paints
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D7/00—Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
- C09D7/40—Additives
- C09D7/66—Additives characterised by particle size
- C09D7/67—Particle size smaller than 100 nm
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
- H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
- H01G11/22—Electrodes
- H01G11/26—Electrodes characterised by their structure, e.g. multi-layered, porosity or surface features
- H01G11/28—Electrodes characterised by their structure, e.g. multi-layered, porosity or surface features arranged or disposed on a current collector; Layers or phases between electrodes and current collectors, e.g. adhesives
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
- H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
- H01G11/22—Electrodes
- H01G11/30—Electrodes characterised by their material
- H01G11/32—Carbon-based
- H01G11/38—Carbon pastes or blends; Binders or additives therein
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
- H01G11/00—Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
- H01G11/84—Processes for the manufacture of hybrid or EDL capacitors, or components thereof
- H01G11/86—Processes for the manufacture of hybrid or EDL capacitors, or components thereof specially adapted for electrodes
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/052—Li-accumulators
- H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/04—Processes of manufacture in general
- H01M4/0402—Methods of deposition of the material
- H01M4/0404—Methods of deposition of the material by coating on electrode collectors
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/04—Processes of manufacture in general
- H01M4/0471—Processes of manufacture in general involving thermal treatment, e.g. firing, sintering, backing particulate active material, thermal decomposition, pyrolysis
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
- H01M4/139—Processes of manufacture
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
- H01M4/621—Binders
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/13—Energy storage using capacitors
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
Definitions
- the present invention relates to a binder composition for an electricity storage device.
- the binder composition for an electricity storage device capable of producing an electrode having better charge / discharge characteristics by intentionally containing a predetermined amount of particles having a predetermined particle diameter in the binder composition instead of removing the particles. Is to provide.
- the present invention has been made to solve at least a part of the above-described problems, and can be realized as the following aspects or application examples.
- a binder composition for an electricity storage device comprising a polymer (A) and a liquid medium (B), wherein 1,000 to 100,000 particles / mL of particles having a particle size of 10 to 50 ⁇ m are contained in the composition. It is contained.
- the polymer (A) can have a repeating unit (Mb) derived from an unsaturated carboxylic acid ester.
- the polymer (A) can be a fluorinated polymer having a repeating unit (Ma) derived from a fluorinated ethylene monomer.
- the polymer (A) is A repeating unit (Md) derived from a conjugated diene compound; A repeating unit (Me) derived from an aromatic vinyl; A repeating unit (Mc) derived from an unsaturated carboxylic acid; It can be a diene polymer having
- the fluorine-containing polymer or the diene polymer may be particles having an average particle diameter of 50 to 400 nm, and the particles may be dispersed in the liquid medium (B).
- One aspect of the method for producing an electrode for an electricity storage device is as follows. Preparing a slurry for an electrode containing a polymer (A), a liquid medium (B), particles having a particle size of 10 to 50 ⁇ m, 1,000 to 100,000 particles / mL, and an electrode active material; Applying the electrode slurry to the current collector surface; Drying the electrode slurry applied to the current collector surface; It is characterized by including.
- the polymer (A) can have a repeating unit (Mb) derived from an unsaturated carboxylic acid ester.
- the polymer (A) can be a fluorinated polymer having a repeating unit (Ma) derived from a fluorinated ethylene monomer.
- the polymer (A) is A repeating unit (Md) derived from a conjugated diene compound; A repeating unit (Me) derived from an aromatic vinyl; A repeating unit (Mc) derived from an unsaturated carboxylic acid; It can be a diene polymer having
- the fluorine-containing polymer or the diene polymer may be particles having an average particle diameter of 50 to 400 ⁇ m, and the particles may be dispersed in the liquid medium (B).
- an electrode for an electricity storage device having excellent charge / discharge characteristics can be produced.
- the reason for this is presumed to be that the electron conductivity in the electrode is improved when particles having a predetermined particle diameter are contained in the composition at a predetermined ratio.
- An electricity storage device including an electrode for an electricity storage device manufactured using the binder composition for an electricity storage device according to the present invention has a good capacity retention rate and can prevent a voltage drop during high-temperature storage.
- (meth) acrylic acid is a concept encompassing both “acrylic acid” and “methacrylic acid”.
- ⁇ (meth) acrylate is a concept encompassing both “ ⁇ acrylate” and “ ⁇ methacrylate”.
- Binder composition for an electricity storage device contains a polymer (A) and a liquid medium (B), and particles having a particle diameter of 10 to 50 ⁇ m in the composition Is 1,000 to 100,000 / mL.
- the polymer (A) preferably has a repeating unit (Mb) derived from an unsaturated carboxylic acid ester in order to improve the adhesion of the electrode active material layer.
- Mb repeating unit
- Polymer (A) The polymer (A) contained in the binder composition for an electricity storage device according to the present embodiment may be dissolved in the liquid medium (B) or in the form of a latex dispersed as particles, A latex is preferred.
- the binder composition for an electricity storage device is in a latex state, the stability of the electrode slurry prepared by mixing with the electrode active material is improved, and the applicability of the electrode slurry to the current collector is improved. preferable.
- the polymer (A) dispersed as particles in the liquid medium (B) is also referred to as “polymer particles (A)”.
- the polymer (A) used in the present embodiment preferably has a repeating unit (Mb) derived from an unsaturated carboxylic acid ester.
- a polymer having a repeating unit (Mb) derived from an unsaturated carboxylic acid ester has good adhesion.
- the unsaturated carboxylic acid ester is preferably a (meth) acrylic acid ester.
- (meth) acrylic acid esters include, for example, methyl (meth) acrylate, ethyl (meth) acrylate, n-propyl (meth) acrylate, i-propyl (meth) acrylate, (meth ) N-butyl acrylate, i-butyl (meth) acrylate, n-amyl (meth) acrylate, i-amyl (meth) acrylate, hexyl (meth) acrylate, cyclohexyl (meth) acrylate, (meth ) 2-ethylhexyl acrylate, n-octyl (meth) acrylate, nonyl (meth) acrylate, decyl (meth) acrylate, hydroxymethyl (meth) acrylate, hydroxyethyl (meth) acryl
- methyl (meth) acrylate at least one selected from methyl (meth) acrylate, ethyl (meth) acrylate, 2-ethylhexyl (meth) acrylate, hydroxymethyl (meth) acrylate and hydroxyethyl (meth) acrylate It is preferable that it is one or more selected from methyl (meth) acrylate, hydroxymethyl (meth) acrylate and hydroxyethyl (meth) acrylate.
- the polymer (A) used in the present embodiment may be a polymer having only a repeating unit (Mb) derived from an unsaturated carboxylic acid ester, or a repeating unit (Mb) derived from an unsaturated carboxylic acid ester. In addition to the above, it may have structural units derived from other copolymerizable unsaturated monomers as described below.
- the content ratio of the repeating unit (Mb) derived from the unsaturated carboxylic acid ester in the polymer (A) used in the present embodiment is preferably 65% by mass or more with respect to the total mass of the polymer (A). More preferably, it is 75 mass% or more.
- the polymer (A) is a repeating unit derived from a fluorine-containing ethylene monomer (Ma).
- Mo fluorine-containing ethylene monomer
- the fluorine-containing polymer that can be used in the present embodiment has a repeating unit (Ma) derived from a fluorine-containing ethylene monomer.
- the fluorine-containing ethylene monomer include olefin compounds having a fluorine atom, (meth) acrylates having a fluorine atom, and the like.
- the olefin compound having a fluorine atom include vinylidene fluoride, tetrafluoroethylene, hexafluoropropylene, ethylene trifluoride chloride, and perfluoroalkyl vinyl ether.
- (meth) acrylate having a fluorine atom for example, a compound represented by the following general formula (1), (meth) acrylic acid 3 [4 [1-trifluoromethyl-2,2-bis [bis (trifluoromethyl) ) Fluoromethyl] ethynyloxy] benzooxy] 2-hydroxypropyl and the like.
- R 1 is a hydrogen atom or a methyl group
- R 2 is a C 1-18 hydrocarbon group containing a fluorine atom.
- R 2 in the general formula (1) examples include a fluorinated alkyl group having 1 to 12 carbon atoms, a fluorinated aryl group having 6 to 16 carbon atoms, and a fluorinated aralkyl group having 7 to 18 carbon atoms. Of these, a fluorinated alkyl group having 1 to 12 carbon atoms is preferable.
- R 2 in the general formula (1) include, for example, 2,2,2-trifluoroethyl group, 2,2,3,3,3-pentafluoropropyl group, 1,1,1, 3,3,3-hexafluoropropan-2-yl group, ⁇ - (perfluorooctyl) ethyl group, 2,2,3,3-tetrafluoropropyl group, 2,2,3,4,4,4- Hexafluorobutyl group, 1H, 1H, 5H-octafluoropentyl group, 1H, 1H, 9H-perfluoro-1-nonyl group, 1H, 1H, 11H-perfluoroundecyl group, perfluorooctyl group, etc. .
- the fluorine-containing ethylene monomer is preferably an olefin compound having a fluorine atom, and more preferably at least one selected from the group consisting of vinylidene fluoride, tetrafluoroethylene and hexafluoropropylene. preferable.
- Said fluorine-containing ethylene-type monomer may be used individually by 1 type, and 2 or more types may be mixed and used for it.
- a polymer (Aa) having a repeating unit (Ma) derived from a fluorine-containing ethylene monomer as a fluorine-containing polymer, and a polymer (Ab) having a repeating unit (Mb) derived from an unsaturated carboxylic acid ester In combination with each other or by polymer alloying, it is possible to express adhesion more effectively without degrading oxidation resistance.
- the polymer (Aa) having the repeating unit (Ma) derived from the fluorine-containing ethylene monomer as the fluorine-containing polymer has only the repeating unit (Ma) derived from the fluorine-containing ethylene monomer.
- it may have a repeating unit derived from another copolymerizable unsaturated monomer other than the repeating unit (Ma) derived from the fluorine-containing ethylene monomer.
- examples of such other unsaturated monomers include a repeating unit (Mb) derived from an unsaturated carboxylic acid ester as described above, a repeating unit (Mc) derived from an unsaturated carboxylic acid described later, and other repeating units.
- a unit etc. can be mentioned and 1 or more types selected from these can be used.
- the content ratio of the repeating unit (Ma) derived from the fluorine-containing ethylene-based monomer in the polymer (Aa) is preferably 80% by mass or more, more preferably based on the total mass of the polymer (Aa). 90% by mass or more.
- the content is preferably 50 to 99% by mass, more preferably 80 to 98% by mass.
- the content ratio is preferably 1 to 50% by mass, more preferably 2 to 20% by mass.
- the polymer (Aa) contains a repeating unit derived from propylene hexafluoride, the content is preferably 1 to 50% by mass, more preferably 2 to 20% by mass.
- the polymer (Aa) can be easily produced by emulsion polymerization of the above fluorine-containing ethylene monomer and optionally another unsaturated monomer according to a known method.
- the fluorine-containing polymer used in the present embodiment preferably has a repeating unit (Mb) derived from an unsaturated carboxylic acid ester.
- a polymer having a repeating unit (Mb) derived from an unsaturated carboxylic acid ester has good adhesion but may have poor oxidation resistance.
- the repeating unit (Ma) derived from the fluorine-containing ethylene monomer and the repeating unit (Mb) derived from the unsaturated carboxylic acid ester in combination it is better while maintaining good adhesion. May exhibit good oxidation resistance.
- the polymer (Ab) having a repeating unit (Mb) derived from an unsaturated carboxylic acid ester may be a polymer having only a repeating unit (Mb) derived from an unsaturated carboxylic acid ester. In addition to the repeating unit (Mb) derived from an ester, it may have a structural unit derived from another copolymerizable unsaturated monomer.
- the content of the repeating unit (Mb) derived from the unsaturated carboxylic acid ester in the fluorinated polymer used in the present embodiment is preferably 50 to 90 mass with respect to the total mass of the polymer (A). %, More preferably 55 to 85% by mass.
- unsaturated carboxylic acid examples include mono- or dicarboxylic acids such as acrylic acid, methacrylic acid, crotonic acid, maleic acid, fumaric acid, itaconic acid, and one or more selected from these. be able to. In particular, at least one selected from acrylic acid, methacrylic acid and itaconic acid is preferable.
- the content ratio of the repeating unit (Mc) derived from the unsaturated carboxylic acid in the fluorinated polymer is preferably 15 parts by mass or less when the total repeating unit is 100 parts by mass, and is 0.3 to 10 parts by mass. More preferably, it is a part.
- the fluorine-containing polymer may have other repeating units.
- Examples of the repeating unit other than the above include ⁇ , ⁇ -unsaturated nitrile compounds, conjugated diene compounds, aromatic vinyl and other unsaturated monomers.
- ⁇ , ⁇ -unsaturated nitrile compound examples include acrylonitrile, methacrylonitrile, ⁇ -chloroacrylonitrile, ⁇ -ethylacrylonitrile, vinylidene cyanide, and the like. Can be. Of these, at least one selected from acrylonitrile and methacrylonitrile is preferable, and acrylonitrile is more preferable.
- the fluorine-containing polymer may further have a repeating unit derived from the compound shown below.
- Examples of such compounds include alkyl amides of ethylenically unsaturated carboxylic acids such as (meth) acrylamide and N-methylol acrylamide; vinyl carboxylic acid esters such as vinyl acetate and vinyl propionate; ethylenically unsaturated dicarboxylic acids.
- Examples include acid anhydrides; monoalkyl esters; monoamides; aminoalkylamides of ethylenically unsaturated carboxylic acids such as aminoethyl acrylamide, dimethylaminomethyl methacrylamide, methylaminopropyl methacrylamide, and the like. Can be one or more.
- the polymer (A) is preferably a diene polymer.
- the diene polymer includes a repeating unit (Md) derived from a conjugated diene compound, a repeating unit (Me) derived from an aromatic vinyl, a repeating unit (Mb) derived from an unsaturated carboxylic acid ester, and an unsaturated carboxylic acid. It is preferable to have a repeating unit (Mc) derived from an acid.
- conjugated diene compound examples include 1,3-butadiene, 2-methyl-1,3-butadiene, 2,3-dimethyl-1,3-butadiene, 2-chloro-1,3-butadiene and the like. , One or more selected from these.
- 1,3-butadiene is particularly preferable.
- the content ratio of the repeating unit (Md) derived from the conjugated diene compound is preferably 30 to 60 parts by mass, and more preferably 40 to 55 parts by mass when all the repeating units are 100 parts by mass.
- the content ratio of the repeating unit (Md) is in the above range, the binding property can be further improved.
- aromatic vinyl examples include styrene, ⁇ -methylstyrene, p-methylstyrene, vinyltoluene, chlorostyrene, divinylbenzene, and the like, and one or more selected from these can be used. Can do. Of the above, the aromatic vinyl is particularly preferably styrene.
- the content of the repeating unit (Me) derived from the aromatic vinyl is preferably 10 to 40 parts by mass, more preferably 15 to 30 parts by mass when the total repeating units are 100 parts by mass.
- the polymer (A) has an appropriate binding property to graphite used as the electrode active material.
- the obtained electrode active material layer is excellent in flexibility and binding property to the current collector.
- the content ratio of the repeating unit (Mb) derived from the unsaturated carboxylic acid ester in the diene polymer is preferably 5 to 40 parts by mass when the total repeating unit is 100 parts by mass. It is more preferable that
- unsaturated carboxylic acid a compound similar to “1.1.2.3. Repeating unit (Mc) derived from unsaturated carboxylic acid” can be used.
- the content of the repeating unit (Mc) derived from the unsaturated carboxylic acid is preferably 15 parts by mass or less when the total repeating unit of the diene polymer is 100 parts by mass, and is 0.3 to 10 parts by mass. It is more preferable that When the content ratio of the repeating unit (Mc) is in the above range, since the dispersion stability is excellent at the time of preparing the electrode slurry, aggregates are hardly generated. Further, an increase in slurry viscosity over time can be suppressed.
- the diene polymer may have other repeating units.
- Examples of the repeating unit other than the above include repeating units derived from ⁇ , ⁇ -unsaturated nitrile compounds.
- ⁇ , ⁇ -unsaturated nitrile compound compounds similar to the ⁇ , ⁇ -unsaturated nitrile compound described in “1.1.2.4. Other Repeating Units” may be used. it can.
- the diene polymer may further have other repeating units described in “1.1.2.4. Other repeating units”.
- diene polymer particles As long as the diene polymer has the above-described configuration, its synthesis method is not particularly limited. For example, a known emulsion polymerization step or an appropriate combination thereof can be easily used. Can be synthesized. For example, it can be easily synthesized by using the method described in Japanese Patent No. 4957932.
- THF insoluble content of the polymer (A) is preferably 80% or more, and more preferably 90% or more.
- the THF-insoluble content is estimated to be approximately proportional to the amount of insoluble content in the electrolytic solution used in the electricity storage device. For this reason, if the THF-insoluble content is in the above range, it is presumed that it is favorable because an electricity storage device is produced and elution of the polymer (A) into the electrolytic solution can be suppressed even when charging and discharging are repeated for a long period of time. it can.
- the polymer (A) is a fluorine-containing polymer, it has only one endothermic peak in the temperature range of ⁇ 50 to 250 ° C. as measured by differential scanning calorimetry (DSC) according to JIS K7121. It is preferable that it does not have.
- the temperature of this endothermic peak is more preferably in the range of ⁇ 30 to + 30 ° C.
- the polymer (Aa) is present alone, it is generally preferable to have an endothermic peak (melting temperature) at ⁇ 50 to 250 ° C.
- the polymer (A) when the polymer (A) is a diene polymer, it has only one endothermic peak in the temperature range of ⁇ 50 to 5 ° C. as measured by differential scanning calorimetry (DSC) according to JIS K7121. It is preferable not to.
- the polymer particles (A) contained in the binder composition for an electricity storage device according to the present embodiment is in the form of latex dispersed as particles in the liquid medium (B), the polymer particles (A) The average particle diameter is preferably in the range of 50 to 400 nm, and more preferably in the range of 100 to 250 nm.
- the average particle diameter of the polymer particles (A) is in the above range, the polymer particles (A) can be sufficiently adsorbed on the surface of the electrode active material. (A) can also follow and move. As a result, it is possible to suppress only one of the two particles from migrating alone, thereby suppressing deterioration of electrical characteristics.
- the average particle size of the polymer particles (A) is the cumulative frequency of the number of particles when the particle size distribution is measured using a particle size distribution measuring apparatus based on the light scattering method and the particles are accumulated from small particles. Is the value of the particle diameter (D50) at which 50%.
- a particle size distribution measuring apparatus include Coulter LS230, LS100, LS13 320 (above, manufactured by Beckman Coulter. Inc.), FPAR-1000 (manufactured by Otsuka Electronics Co., Ltd.), and the like. These particle size distribution measuring devices are not intended to evaluate only the primary particles of the polymer particles, but can also evaluate the secondary particles formed by aggregation of the primary particles.
- the particle size distribution measured by these particle size distribution measuring devices can be used as an indicator of the dispersion state of the polymer particles contained in the electrode slurry.
- the average particle size of the polymer particles (A) is also measured by a method in which the electrode slurry is centrifuged to precipitate the electrode active material, and then the supernatant is measured by the above particle size distribution measuring apparatus. Can do.
- the binder composition for an electricity storage device according to the present embodiment contains a liquid medium (B).
- the liquid medium (B) is preferably an aqueous medium containing water.
- the aqueous medium can contain a non-aqueous medium other than water. Examples of the non-aqueous medium include amide compounds, hydrocarbons, alcohols, ketones, esters, amine compounds, lactones, sulfoxides, sulfone compounds, and the like. Use one or more selected from these. Can do.
- the liquid medium (B) contains water and a non-aqueous medium other than water, 90% by mass or more is preferably water, and 98% by mass or more in the total amount of 100% by mass of the liquid medium (B). More preferably, is water.
- the binder composition for an electricity storage device according to the present embodiment has a low degree of adverse effects on the environment, and is also safer for handling workers.
- the content ratio of the non-aqueous medium contained in the aqueous medium is preferably 10 parts by mass or less, more preferably 5 parts by mass or less, and substantially no content with respect to 100 parts by mass of the aqueous medium. Is particularly preferred.
- “substantially does not contain” means that a non-aqueous medium is not intentionally added as the liquid medium (B), and is inevitably mixed when a binder composition for an electricity storage device is produced. Non-aqueous media may be included.
- the binder composition for electrical storage devices which concerns on this Embodiment can contain additives other than the polymer (A) mentioned above and a liquid medium (B) as needed. Examples of such additives include preservatives and thickeners.
- the binder composition for an electricity storage device according to the present embodiment is further improved in storage stability by containing a preservative, and by containing a thickener, its applicability and charge / discharge of the obtained electricity storage device. Characteristics and the like can be further improved.
- the binder composition for electrical storage devices which concerns on this Embodiment can contain antiseptic
- preservative by adding an isothiazoline-based compound as a preservative to the binder composition for an electricity storage device, the storage of the binder composition for an electricity storage device suppresses the generation of foreign substances due to growth of bacteria, sputum, etc. Can do.
- deterioration of the binder is suppressed during charging / discharging of the electricity storage device, it is possible to suppress a decrease in charge / discharge characteristics of the electricity storage device.
- thickener for example, cellulose compounds such as carboxymethylcellulose, methylcellulose, hydroxypropylcellulose; ammonium salts or alkali metal salts of the above cellulose compounds; poly (meth) acrylic acid, modified poly (meth) acrylic acid, etc. Polycarboxylic acids of the above; alkali metal salts of the above polycarboxylic acids; polyvinyl alcohol (co) polymers such as polyvinyl alcohol, modified polyvinyl alcohol, ethylene-vinyl alcohol copolymers; (meth) acrylic acid, maleic acid and fumaric acid And water-soluble polymers such as saponified products of copolymers of unsaturated carboxylic acids and vinyl esters.
- particularly preferable thickeners are alkali metal salts of carboxymethyl cellulose, poly (meth) acrylic acid and alkali metal salts thereof.
- Examples of commercially available products of these thickeners include alkali metal salts of carboxymethyl cellulose such as CMC1120, CMC1150, CMC2200, CMC2280, and CMC2450 (manufactured by Daicel Corporation).
- the use ratio of the thickener is 5% by mass or less with respect to the total solid content of the binder composition for an electricity storage device. Is more preferable, and 0.1 to 3% by mass is more preferable.
- the binder composition for an electricity storage device contains particles having a particle diameter of 10 to 50 ⁇ m in the composition.
- the content of particles having a particle size of 10 to 50 ⁇ m in the binder composition for an electricity storage device is 1,000 to 100,000 particles / mL, preferably 1,000 to 50,000 particles / mL, More preferably, it is 1,000 to 10,000 / mL.
- an electrode slurry prepared using the binder composition for an electricity storage device is applied to a current collector.
- An electricity storage device including the prepared electrode exhibits good charge / discharge characteristics.
- the binder composition for an electricity storage device contains particles having a particle size of 10 to 50 ⁇ m in an amount of 1,000 to 100,000 particles / mL
- an electrode produced using this binder composition for an electricity storage device Particles having a particle size of 10 to 50 ⁇ m remain also in the electrode active material layer produced by applying and drying the slurry to the current collector.
- an electrode including such an electrode active material layer non-uniform pores are formed in the active material layer by particles having a particle diameter of 10 to 50 ⁇ m, and it is presumed that penetration of the electrolyte solution is promoted.
- the mobility of ions responsible for charge transfer, such as lithium ions is improved, and the charge / discharge characteristics of the electricity storage device can be improved.
- the particles having a particle size of 10 to 50 ⁇ m contained in the binder composition for an electricity storage device according to the present embodiment may be any material that does not occlude and release lithium ions, such as an active material. Particles are preferred.
- metal particles and oxide particles examples include iron, titanium (titania), aluminum (alumina), zirconium (zirconia), magnesium (magsia), oxides of these metals, silica, and stainless steel (SUS201, 202, 301, 302). , 303, 304, 305, 316, 317, 403, 405, 420, 430, 630, etc.) can be used.
- iron, stainless steel, titanium (titania), and aluminum (alumina) are preferable from the viewpoint of further improving the toughness of the active material layer.
- titania rutile type titanium oxide is more preferable from the viewpoint of further improving the toughness of the active material layer.
- the particle diameter of the particles contained in the binder composition for an electricity storage device may be 10 to 50 ⁇ m, and is preferably in the range of 10 to 20 ⁇ m.
- the particle diameter of the particles is preferably smaller than the thickness of the active material layer. Thereby, it can avoid that a particle
- the particle size of the particles and the content in the binder composition for the electricity storage device are measured when the particle size distribution is measured using a particle size distribution measuring apparatus based on the laser diffraction method, and the particles are accumulated from small particles.
- Examples of such a laser diffraction particle size distribution measuring apparatus include HORIBA LA-300 series, HORIBA LA-920 series (above, manufactured by Horiba, Ltd.), and the like. This particle size distribution measuring apparatus does not only evaluate the primary particles of the particles, but also evaluates the secondary particles formed by aggregation of the primary particles.
- the particle diameter obtained by this particle size distribution measuring apparatus can be used as an indicator of the dispersion state of the particles contained in the composition for an electricity storage device.
- the particle diameter of the particles can also be measured by centrifuging the power storage device composition to precipitate the particles, removing the supernatant liquid, and measuring the precipitated particles by the above method. .
- Electrode slurry can be produced using the above-mentioned binder composition for an electricity storage device.
- the electrode slurry is a dispersion used to form an electrode active material layer on the current collector surface after being applied to the current collector surface and then dried.
- the electrode slurry according to the present embodiment contains the above-described binder composition for an electricity storage device and an electrode active material.
- each component contained in the electrode slurry according to the present embodiment will be described in detail. However, since the binder composition for an electricity storage device is as described above, the description thereof is omitted.
- Electrode active material There is no restriction
- Oxide in the present specification is a concept that means a compound or salt composed of oxygen and an element having an electronegativity lower than that of oxygen.
- metal oxide metal phosphate, nitrate, This concept also includes halogen oxoacid salts, sulfonic acid salts, and the like.
- lithium atom-containing oxide examples include a composite metal oxide represented by the following general formula (3a) or (3b), and a lithium atom-containing oxide represented by the following general formula (4) and having an olivine crystal structure. It is preferable to use at least one selected from the group consisting of these.
- M 1 is at least one metal atom selected from the group consisting of Co, Ni and Mn
- M 2 is at least one selected from the group consisting of Al and Sn) Is a metal atom of the species
- O is an oxygen atom
- x, y and z are in the range of 0.10 ⁇ x ⁇ 0, 4.00 ⁇ y ⁇ 0.85 and 2.00 ⁇ z ⁇ 0, respectively Is the number of Li 1-x M 3 x (XO 4 ) (4)
- M 3 is a metal selected from the group consisting of Mg, Ti, V, Nb, Ta, Cr, Mn, Fe, Co, Ni, Cu, Zn, Al, Ga, Ge, and Sn.
- X is at least one selected from the group consisting of Si, S, P and V; x is a number and satisfies the relationship 0 ⁇ x ⁇ 1.)
- the value of x in the general formula (4) is selected so that the valence of the entire general formula (4) is 0 in accordance with the valences of M 3 and X, respectively.
- the lithium atom-containing oxide represented by the general formula (4) and having an olivine crystal structure has different electrode potentials depending on the type of the metal element M 3 . Therefore, the battery voltage can be arbitrarily set by selecting the type of the metal element M.
- the lithium atom-containing oxide having an olivine crystal structure LiFePO 4 , LiCoPO 4 , Li 0.90 Ti 0.05 Nb 0.05 Fe 0.30 Co 0.30 Mn 0.30 PO 4 And so on.
- LiFePO 4 is particularly preferable because it is easy to obtain an iron compound as a raw material and is inexpensive.
- the compound which substituted Fe ion in said compound by Co ion, Ni ion, or Mn ion also has the same crystal structure as said each compound, it has the same effect as an electrode active material.
- carbon when producing a negative electrode of a lithium ion secondary battery, for example, carbon can be used as the electrode active material (negative electrode active material).
- specific examples of carbon include carbon materials obtained by firing organic polymer compounds such as phenol resin, polyacrylonitrile, and cellulose; carbon materials obtained by firing coke and pitch; artificial graphite; natural graphite and the like Can be mentioned.
- activated carbon activated carbon fiber, silica, alumina or the like can be used as the electrode active material.
- carbon materials such as graphite, non-graphitizable carbon, hard carbon, coke, polyacene organic semiconductor (PAS), or the like can be used.
- the average particle diameter (Db) of the electrode active material is preferably in the range of 0.4 to 10 ⁇ m and more preferably in the range of 0.5 to 7 ⁇ m for the positive electrode.
- the negative electrode it is preferably in the range of 3 to 30 ⁇ m, more preferably in the range of 5 to 25 ⁇ m.
- the electrode slurry contains a conductivity-imparting agent described later
- the contact area between the electrode active material and the conductivity-imparting agent is sufficiently ensured by the average particle diameter (Db) of the electrode active material being within the above range.
- Db average particle diameter
- the average particle diameter (Db) of the electrode active material is a particle size distribution measuring apparatus using a laser diffraction method as a measurement principle, and the cumulative frequency when particles are accumulated from small particles is 50. % Particle diameter (D50).
- a laser diffraction particle size distribution measuring apparatus examples include HORIBA LA-300 series, HORIBA LA-920 series (above, manufactured by Horiba, Ltd.), and the like.
- This particle size distribution measuring apparatus is not intended to evaluate only the primary particles of the electrode active material, but also evaluates the secondary particles formed by aggregation of the primary particles. Therefore, the average particle diameter (Db) obtained by this particle size distribution measuring apparatus can be used as an indicator of the dispersion state of the electrode active material contained in the electrode slurry.
- the average particle diameter (Db) of the electrode active material is measured by centrifuging the electrode slurry to settle the electrode active material, then removing the supernatant and measuring the precipitated electrode active material by the above method. Can also be measured.
- the electrode slurry can contain components other than the components described above as necessary. Examples of such components include a conductivity-imparting agent, water, a non-aqueous medium, and a thickener.
- conductivity-imparting agent examples include carbon in a lithium ion secondary battery; in a nickel-hydrogen secondary battery, cobalt oxide at the positive electrode: nickel powder, cobalt oxide, titanium oxide, carbon at the negative electrode Etc. are used respectively.
- examples of carbon include graphite, activated carbon, acetylene black, furnace black, graphite, carbon fiber, and fullerene. Among these, acetylene black or furnace black can be preferably used.
- the use ratio of the conductivity-imparting agent is preferably 20 parts by mass or less, more preferably 1 to 15 parts by mass, and particularly preferably 2 to 10 parts by mass with respect to 100 parts by mass of the electrode active material.
- the electrode slurry may contain a non-aqueous medium having a standard boiling point of 80 to 350 ° C. from the viewpoint of improving the coating property.
- a non-aqueous medium include amide compounds such as N-methylpyrrolidone, dimethylformamide, N, N-dimethylacetamide; hydrocarbons such as toluene, xylene, n-dodecane and tetralin; 2-ethyl- Alcohols such as 1-hexanol, 1-nonanol and lauryl alcohol; ketones such as methyl ethyl ketone, cyclohexanone, phorone, acetophenone and isophorone; esters such as benzyl acetate, isopentyl butyrate, methyl lactate, ethyl lactate and butyl lactate; o-toluidine, m -Amine compounds such as toluidine and p-tolui
- the said electrode slurry can contain a thickener from a viewpoint of improving the coating property.
- Specific examples of the thickener include various compounds described in the above “1.3.2. Thickener”.
- the use ratio of the thickener is preferably 20% by mass or less, more preferably 0.1 to 15% by mass with respect to the total solid content of the electrode slurry. %, Particularly preferably 0.5 to 10% by mass.
- the electrode slurry according to the present embodiment is manufactured by mixing the above-mentioned binder composition for an electricity storage device, an electrode active material, and an additive used as necessary. Can do. These mixing can be performed by stirring by a known method, and for example, a stirrer, a defoamer, a bead mill, a high-pressure homogenizer, or the like can be used.
- the preparation of the electrode slurry (mixing operation of each component) is preferably performed at least part of the process under reduced pressure. Thereby, it can prevent that a bubble arises in the electrode layer obtained.
- the degree of pressure reduction is preferably about 5.0 ⁇ 10 3 to 5.0 ⁇ 10 5 Pa as an absolute pressure.
- the mixing and stirring for producing the slurry for electrodes it is necessary to select a mixer capable of stirring to such an extent that no agglomerates of the electrode active material remain in the slurry and sufficient dispersion conditions as necessary.
- the degree of dispersion can be measured by a particle gauge, but it is preferable to mix and disperse so that aggregates larger than at least 100 ⁇ m are eliminated.
- the mixer that meets such conditions include a ball mill, a sand mill, a pigment disperser, a crusher, an ultrasonic disperser, a homogenizer, a planetary mixer, and a Hobart mixer.
- the electrode slurry according to the present embodiment preferably has a solid content concentration (the ratio of the total mass of components other than the solvent in the slurry to the total mass of the slurry) of 20 to 80% by mass, More preferably, it is ⁇ 75% by mass.
- Electrode The electrode according to the present embodiment includes a current collector and a layer formed by applying and drying the aforementioned electrode slurry on the surface of the current collector.
- Such an electrode is manufactured by applying the above-mentioned electrode slurry to the surface of an appropriate current collector such as a metal foil to form a coating film, and then drying the coating film to form an electrode active material layer. can do.
- the electrode produced in this manner is an electrode containing the above-mentioned polymer (A), particles having a particle diameter of 10 to 50 ⁇ m, an electrode active material, and optional components added as necessary on a current collector.
- the active material layer is bound.
- Such an electrode has excellent binding properties between the current collector and the electrode active material layer, and also has good charge / discharge rate characteristics, which is one of electrical characteristics. Therefore, such an electrode is suitable as an electrode for an electricity storage device.
- the method for producing an electricity storage device electrode includes (1) a polymer (A), a liquid medium (B), 1,000 to 100,000 particles / mL of particles having a particle size of 10 to 50 ⁇ m, A step of preparing an electrode slurry containing an electrode active material; (2) a step of applying the electrode slurry to a current collector surface; and (3) an electrode slurry applied to the current collector surface. Drying.
- the current collector is not particularly limited as long as it is made of a conductive material.
- a current collector made of metal such as iron, copper, aluminum, nickel, and stainless steel is used.
- the above-mentioned electrode binder is used. The effect of the slurry for an electrode manufactured using is best exhibited.
- a punching metal, an expanded metal, a wire mesh, a foam metal, a mesh metal fiber sintered body, a metal plated resin plate, or the like is used as the current collector in the nickel metal hydride secondary battery.
- the shape and thickness of the current collector are not particularly limited, but it is preferable that the current collector be a sheet having a thickness of about 0.001 to 0.5 mm.
- the coating can be performed by an appropriate method such as a doctor blade method, a dip method, a reverse roll method, a direct roll method, a gravure method, an extrusion method, a dipping method, or a brush coating method.
- the coating amount of the electrode slurry is not particularly limited, but the thickness of the electrode active material layer formed after removing the liquid medium (concept including both water and a non-aqueous medium that is optionally used) is not limited. The amount is preferably 0.005 to 5 mm, and more preferably 0.01 to 2 mm. When the thickness of the electrode active material layer is within the above range, the electrode active material layer can be effectively infiltrated with the electrolytic solution.
- the metal ions accompanying the charge / discharge between the electrode active material in the electrode active material layer and the electrolytic solution are easily exchanged, which is preferable because the electrode resistance can be further reduced.
- the electrode active material layer since the thickness of the electrode active material layer is within the above range, the electrode active material layer does not peel from the current collector even when the electrode is processed by folding or winding. Is preferable in that an electrode for an electricity storage device having good flexibility and high flexibility can be obtained.
- drying method from the coated film after coating (method for removing water and optionally used non-aqueous medium); for example, drying with warm air, hot air, low humidity air; vacuum drying; (far) infrared , Drying by irradiation with an electron beam or the like.
- the drying speed is appropriately set so that the liquid medium can be removed as quickly as possible within a speed range in which the electrode active material layer does not crack due to stress concentration or the electrode active material layer does not peel from the current collector. Can be set.
- the pressing method includes a die press and a roll press.
- the pressing conditions should be appropriately set depending on the type of press equipment used and the desired values of the porosity and density of the electrode active material layer. This condition can be easily set by a few preliminary experiments by those skilled in the art.
- the linear pressure of the roll press machine is 0.1 to 10 (t / cm), preferably 0.
- the current collector feed speed (roll rotation speed) after drying is 1 to 80 m / min, preferably 5 to 50 m / min. It can be performed in min.
- the density of the electrode active material layer after pressing is preferably 1.5 to 5.0 g / cm 3 , more preferably 1.5 to 4.0 g / cm 3, and 1.6 to 3. Particularly preferred is 8 g / cm 3 .
- the density of the electrode active material layer is preferably 2.0 to 4.0 g / cm 3. 3.0 to 3.5 g / cm 3 is more preferable.
- the density of the electrode active material layer may be 1.5 to 2.5 g / cm 3.
- the density of the electrode active material layer is in the above range, more preferably 1.7 to 2.2 g / cm 3 , further preferably 1.8 to 2.1 g / cm 3. Particularly preferred.
- the density of the electrode active material layer is in the above range, the binding property between the current collector and the electrode active material layer is improved, and an electrode having excellent powdering properties and electrical characteristics is obtained. Will be.
- the porosity of the electrode active material layer after pressing is preferably 10 to 50%, more preferably 15 to 45%, and particularly preferably 20 to 40%.
- the porosity of the electrode active material layer is in the above range, the binding property between the current collector and the electrode active material layer is good, and an electrode having excellent powdering properties and electrical characteristics is obtained. It is done.
- the porosity of the electrode active material layer is within the above range, the electrolyte solution can be sufficiently infiltrated into the electrode active material layer, and the surface of the electrode active material and the electrolyte solution can be sufficiently in contact with each other. As a result, it becomes easy to exchange the lithium ions of the electrode active material and the electrolytic solution, and good charge / discharge characteristics can be achieved.
- the power storage device includes the above-described electrode, and further contains an electrolytic solution, and can be manufactured according to a conventional method using components such as a separator.
- a negative electrode and a positive electrode are overlapped via a separator, and this is wound into a battery container according to a battery shape, put into a battery container, an electrolyte is injected into the battery container, and sealing is performed.
- the method of doing is mentioned.
- the shape of the battery can be an appropriate shape such as a coin shape, a button shape, a sheet shape, a cylindrical shape, a square shape, or a flat shape.
- the electrolytic solution may be liquid or gel, and a material that effectively expresses the function as a battery may be selected from known electrolytic solutions used for the electricity storage device according to the type of the electrode active material.
- the electrolytic solution can be a solution in which an electrolyte is dissolved in a suitable solvent.
- any conventionally known lithium salt can be used, and specific examples thereof include, for example, LiClO 4 , LiBF 4 , LiPF 6 , LiCF 3 CO 2 , LiAsF. 6 , LiSbF 6 , LiB 10 Cl 10 , LiAlCl 4 , LiCl, LiBr, LiB (C 2 H 5 ) 4, LiCF 3 SO 3 , LiCH 3 SO 3 , LiC 4 F 9 SO 3 , Li (CF 3 SO 2 ) 2 N, lithium of lower fatty acid carboxylate etc. can be illustrated.
- the solvent for dissolving the electrolyte is not particularly limited, but specific examples thereof include carbonate compounds such as propylene carbonate, ethylene carbonate, butylene carbonate, dimethyl carbonate, methyl ethyl carbonate, and diethyl carbonate; Lactone compounds such as butyl lactone; ether compounds such as trimethoxymethane, 1,2-dimethoxyethane, diethyl ether, 2-ethoxyethane, tetrahydrofuran, 2-methyltetrahydrofuran; sulfoxide compounds such as dimethyl sulfoxide; One or more selected from these can be used.
- the concentration of the electrolyte in the electrolytic solution is preferably 0.5 to 3.0 mol / L, more preferably 0.7 to 2.0 mol / L.
- Synthesis example 1 5.1.1. Preparation of polymer (A) After the inside of an autoclave having an internal volume of about 6 L equipped with an electromagnetic stirrer was sufficiently purged with nitrogen, 2.5 L of deoxygenated pure water and 25 g of ammonium perfluorodecanoate as an emulsifier were charged. The temperature was raised to 60 ° C. while stirring at 350 rpm. Next, a mixed gas composed of 70% of vinylidene fluoride (VDF) as a monomer and 30% of propylene hexafluoride (HFP) was charged until the internal pressure reached 20 kg / cm 2 .
- VDF vinylidene fluoride
- HFP propylene hexafluoride
- Emulsifier “ADEKA rear soap SR1025” (trade name, manufactured by ADEKA Corporation) 0.5 part by mass, methyl methacrylate (MMA) 30 parts by mass, 2-ethylhexyl acrylate (EHA) 40 parts by mass and methacrylic acid (MAA) 5 parts by mass and 130 parts by mass of water were sequentially added, and the mixture was stirred at 70 ° C. for 3 hours to allow the polymer (Aa) to absorb the monomer.
- THF insoluble matter (%) ((1-Y) / 1) ⁇ 100 (9) Further, when the obtained fine particles were measured by a differential scanning calorimeter (DSC), only one single glass transition temperature Tg was observed at ⁇ 5 ° C. Despite the use of two types of polymers, the obtained polymer particles (A) show only one Tg, so it can be assumed that the polymer (A) is a polymer alloy.
- the particle size distribution is measured using a particle size distribution measuring apparatus (manufactured by Otsuka Electronics Co., Ltd., type “FPAR-1000”) based on the dynamic light scattering method.
- FPAR-1000 particle size distribution measuring apparatus
- Synthesis Examples 2 to 7 and Synthesis Example 11 Compositions shown in Table 1 are the same as those in Synthesis Example 1 except that the composition of the monomers and the amount of the emulsifier are appropriately changed in “5.1.1. Production of polymer (A)” in Synthesis Example 1. An aqueous dispersion containing the polymer (A) was prepared, and water was removed under reduced pressure or added according to the solid content concentration of the aqueous dispersion to obtain an aqueous dispersion having a solid content concentration of 40%. When the fine particles obtained in Synthesis Examples 2 to 7 and Synthesis Example 11 were measured with a differential scanning calorimeter (DSC), only one single glass transition temperature Tg was observed at the temperature shown in Table 1. . In spite of using two types of polymers, since the obtained polymer (A) shows only one Tg, it can be estimated that the polymer (A) is a polymer alloy.
- DSC differential scanning calorimeter
- Synthesis Example 8 A separable flask having a volume of 7 liters was charged with 150 parts by mass of water and 0.2 parts by mass of sodium dodecylbenzenesulfonate, and the inside of the separable flask was sufficiently purged with nitrogen.
- ether sulfate type emulsifier (trade name “ADEKA rear soap SR1025”, manufactured by ADEKA Co., Ltd.) as an emulsifier, 0.8 parts by mass in terms of solid content, and 2, 2,2-trifluoroethyl methacrylate (TFEMA) 20 parts by mass, acrylonitrile (AN) 10 parts by mass, methyl methacrylate (MMA) 25 parts by mass, 2-ethylhexyl acrylate (EHA) 40 parts by mass and acrylic acid (AA) 5 parts by mass
- TFEMA 2, 2,2-trifluoroethyl methacrylate
- AN acrylonitrile
- MMA methyl methacrylate
- EHA 2-ethylhexyl acrylate
- acrylic acid AA
- the temperature inside the separable flask was started, and when the temperature inside the separable flask reached 60 ° C., 0.5 parts by mass of ammonium persulfate was added as a polymerization initiator. Then, when the temperature inside the separable flask reaches 70 ° C., the addition of the monomer emulsion prepared above is started, and the temperature inside the separable flask is maintained at 70 ° C. The emulsion was added slowly over 3 hours. Thereafter, the temperature inside the separable flask was raised to 85 ° C., and this temperature was maintained for 3 hours to carry out the polymerization reaction. After 3 hours, the separable flask was cooled to stop the reaction, and ammonium water was added to adjust the pH to 7.6 to obtain an aqueous dispersion containing 30% of the polymer particles (A). .
- a polymer composition F8 was produced in the same manner as in Synthesis Example 1 except that the aqueous dispersion obtained above was used.
- Synthesis Examples 9 to 10 A water-based dispersion containing the polymer (A) shown in Table 1 was obtained in the same manner as in Synthesis Example 8 except that the type and amount (parts) of each monomer were as shown in Table 1. It was. Polymer compositions F9 to F10 were produced in the same manner as in Synthesis Example 1 except that the aqueous dispersion thus obtained was used.
- VDF vinylidene fluoride
- HFP propylene hexafluoride
- TFEMA 2,2,2-trifluoroethyl methacrylate
- TFEA 2,2,2-trifluoroethyl acrylate
- HFIPA acrylic acid 1,1, 1,3,3,3-hexafluoroisopropyl
- MMA methyl methacrylate
- EHA 2-ethylhexyl acrylate
- MAA methacrylic acid
- AA acrylic acid
- DVB divinylbenzene
- TMPTMA trimethylolpropane trimethacrylate
- AN Acrylonitrile
- Synthesis Example 12 In a temperature-controllable autoclave equipped with a stirrer, 200 parts by weight of water, 0.9 parts by weight of sodium dodecylbenzenesulfonate, 1.0 part by weight of potassium persulfate, 0.5 parts by weight of sodium bisulfite, ⁇ -methylstyrene 0.2 parts by mass of dimer, 0.2 parts by mass of dodecyl mercaptan, and the first stage polymerization component shown in Table 3 were charged all at once, and the temperature was raised to 70 ° C. to carry out the polymerization reaction for 2 hours.
- the second-stage polymerization component shown in Table 3 was added over 6 hours while maintaining the reaction temperature at 70 ° C.
- 3 hours passed from the start of addition of the second stage polymerization component 1.0 part by mass of ⁇ -methylstyrene dimer and 0.3 part by mass of dodecyl mercaptan were added.
- the temperature was raised to 80 ° C. the reaction was further continued for 2 hours.
- the latex pH was adjusted to 7.5, and 5 parts by mass of sodium tripolyphosphate (in terms of solid content) was added. Thereafter, the residual monomer was treated with steam distillation and concentrated under reduced pressure to a solid content of 50% to obtain an aqueous dispersion containing 50% of the polymer (A).
- a polymer composition S1 was produced in the same manner as in Synthesis Example 1 except that the aqueous dispersion obtained above was used.
- Synthesis Examples 13-24 The type and amount (parts) of each monomer are as shown in Table 2, and the content ratio of the first stage polymerization component and the second stage polymerization component when producing the polymer (A) is as shown in Table 3.
- aqueous dispersions containing the polymer (A) shown in Table 2 were obtained.
- Polymer compositions S2 to S13 were produced in the same manner as in Synthesis Example 1 except that the aqueous dispersion thus obtained was used.
- MMA methyl methacrylate
- HEMA 2-hydroxyethyl methacrylate
- AA acrylic acid
- TA itaconic acid
- AN acrylonitrile
- BD 1,3-butadiene
- ST styrene
- Synthesis Example 25 The interior of an autoclave with an internal volume of about 6 liters equipped with an electromagnetic stirrer was sufficiently purged with nitrogen, then charged with 2.5 liters of deoxygenated pure water and 25 g of ammonium perfluorodecanoate as an emulsifier, and stirred at 350 rpm. The temperature was raised to 60 ° C. Next, a mixed gas composed of 44.2% vinylidene fluoride (VDF) and 55.8% propylene hexafluoride (HFP) was charged until the internal pressure reached 20 kg / cm 2 G.
- VDF vinylidene fluoride
- HFP propylene hexafluoride
- NMP corresponding to 900 parts by mass was added to the aqueous dispersion with respect to 100 parts by mass (in terms of solid content) of the obtained aqueous dispersion.
- water was distilled off under reduced pressure conditions to obtain an NMP solution of the polymer (A).
- the amounts of addition of the polymer (A) and the preservative are the types and addition amounts shown in Table 4, and the aqueous dispersion is used instead.
- a polymer composition F12 was produced in the same manner as in Synthesis Example 1 except that the NMP solution of the polymer (A) was used.
- Synthesis Examples 26-30 The types and charge amounts (parts by mass) of the respective monomers are as shown in Table 4, and the content ratios of the first-stage polymerization component and the second-stage polymerization component when producing the polymer (A) are as shown in Table 4. NMP solutions containing the polymer (A) listed in Table 4 were obtained in the same manner as in Synthesis Example 25 except that Polymer compositions F13 to F17 were produced in the same manner as in Synthesis Example 25 except that the NMP solution thus obtained was used.
- VDF vinylidene fluoride
- HFP propylene hexafluoride
- nBA n-butyl acrylate
- MMA methyl methacrylate
- ST styrene
- IA itaconic acid
- ATBS 2-acrylamido-2-methylpropanesulfonic acid
- NMAM N-methylolacrylamide
- NASS sodium styrenesulfonate
- GMA glycidyl methacrylate
- the polymer composition F18 is PVdF (manufactured by Kureha Battery Materials Japan, model number # 7305, 5% NMP solution, molecular weight of 1 million or more) instead of the polymer used in Synthesis Example 25. This was prepared in the same manner as in Synthesis Example 25 except that the NMP solution was used.
- Example 1 5.9.1. Preparation of binder composition for electricity storage device To the polymer composition F1 prepared in “5.1.2. Preparation of polymer composition”, iron powder of 20 ⁇ m or less previously classified by sieving was added. , Stirred. The mixture thus prepared was passed through a magnet filter (magnetic force: 1.7 T, flow rate: 15 kg / min) to remove coarse iron powder. About the obtained binder composition for electrical storage devices, the particle size and number of iron powder were confirmed with the microscope.
- a magnet filter magnet filter
- Electrode slurry 1 part by weight of a thickener (trade name “CMC1120”, manufactured by Daicel Corporation) in a biaxial planetary mixer (product name “TK Hibismix 2P-03” manufactured by PRIMIX Corporation) Conversion), 100 parts by mass of an electrode active material having a particle diameter (D50 value) of 0.5 ⁇ m obtained by pulverizing commercially available lithium iron phosphate (LiFePO 4 ) in an agate mortar and classifying with a sieve. 5 parts by mass of acetylene black and 68 parts by mass of water were added and stirred at 60 rpm for 1 hour. Subsequently, the binder composition for an electricity storage device obtained in the above “5.9.1.
- a thickener trade name “CMC1120”, manufactured by Daicel Corporation
- TK Hibismix 2P-03 manufactured by PRIMIX Corporation
- binder composition for an electricity storage device Production of binder composition for an electricity storage device” is used so that the polymer particles contained in the composition are 1 part by mass.
- the mixture was further stirred for 1 hour to obtain a paste.
- Water was added to the obtained paste to adjust the solid content concentration to 50%, and then the mixture was stirred at 200 rpm for 2 minutes using a stirring defoamer (trade name “Awatori Nertaro” manufactured by Shinky Co., Ltd.).
- the mixture was stirred and mixed at 1,800 rpm for 1.5 minutes at 800 rpm for 5 minutes and further under vacuum (about 5.0 ⁇ 10 3 Pa) to prepare an electrode slurry.
- the electrode slurry prepared in the above “5.9.2. Preparation of electrode slurry” had a thickness of 100 ⁇ m after drying. The mixture was uniformly applied by a doctor blade method and dried at 120 ° C. for 20 minutes. Then, the electrode (positive electrode) for electrical storage devices was obtained by pressing with a roll press machine so that the density of a film
- the counter electrode (negative electrode) slurry prepared above was uniformly applied to the surface of the current collector made of copper foil by the doctor blade method so that the film thickness after drying was 150 ⁇ m, and dried at 120 ° C. for 20 minutes. . Then, the counter electrode (negative electrode) was obtained by pressing using a roll-press machine so that the density of a film
- ⁇ Assembly of lithium-ion battery cells> A bipolar coin cell (manufactured by Hosen Co., Ltd.) manufactured by punching and molding the electrode (negative electrode) produced in the above to a diameter of 15.95 mm in an Ar-substituted glove box with a dew point of ⁇ 80 ° C. or lower.
- a lithium ion battery cell (power storage device) was assembled by placing the positive electrode manufactured in the above-described method by punching and molding the positive electrode to a diameter of 16.16 mm, and sealing the outer body of the bipolar coin cell with a screw.
- “1C” indicates a current value at which discharge is completed in one hour after constant-current discharge of a cell having a certain electric capacity.
- “0.1 C” is a current value at which discharge is completed over 10 hours
- “10 C” is a current value at which discharge is completed over 0.1 hours.
- the lithium ion secondary battery produced above was charged at a constant current (1 C) at 25 ° C., and continued to be charged at a constant voltage (4.2 V) when the voltage reached 4.2 V.
- the charging was completed when the current value reached 0.01C.
- After measuring the battery voltage of the battery it was put in a container with an insulating partition (in this example, a PP container) and placed in a constant temperature bath at 60 ° C. and stored for 2 weeks. Then, it took out and left still in a 25 degreeC thermostat, and the battery voltage was measured 3 hours afterward.
- the measured voltage drop (mV) at high temperature is also shown in Table 5. When the voltage drop is 50 mV or less, it can be judged as good.
- Examples 2 to 26 and Comparative Examples 1 to 6 The binder composition for an electricity storage device in the same manner as in Example 1 except that the polymer composition and conditions shown in Table 5 were used in “5.9.1. Production of binder composition for an electricity storage device” in Example 1. Then, an electrode for an electricity storage device and an electricity storage device were prepared and evaluated. The results are also shown in Table 5. In addition, also about SUS powder (SUS430), it carried out similarly to Example 1, adding the SUS powder of 20 micrometers or less previously classified by the sieve, passing the magnet filter, and removing the coarse SUS grain.
- SUS powder SUS430
- Example 27 5.11.1. Preparation of binder composition for electricity storage device A binder composition for electricity storage device was produced in the same manner as in Example 1 except that the composition and conditions shown in Table 6 were used.
- the electrode slurry prepared in the above-mentioned “5.1.2. Preparation of electrode slurry” had a film thickness after drying of 80 ⁇ m. Then, it was uniformly coated by a doctor blade method and dried at 120 ° C. for 20 minutes. Then, the electrode (negative electrode) was obtained by pressing with a roll press so that the density of an electrode layer might be set to 1.5 g / cm ⁇ 3 >.
- ⁇ Assembly of lithium-ion battery cells> A bipolar coin cell (manufactured by Hosen Co., Ltd.) manufactured by punching and molding the electrode (negative electrode) produced in the above to a diameter of 15.95 mm in an Ar-substituted glove box with a dew point of ⁇ 80 ° C. or lower.
- a lithium ion battery cell (power storage device) was assembled by placing the positive electrode manufactured in the above-described method by punching and molding the positive electrode to a diameter of 16.16 mm, and sealing the outer body of the bipolar coin cell with a screw.
- Example 54 except that polyacrylic acid (manufactured by ACROS, product number “185012500”, average molecular weight 240,000) was used instead of the polymer used in Synthesis Example 1, the same procedure as in Synthesis Example 1 was used. Polymer composition S14 was produced, and an electrode for an electricity storage device and an electricity storage device were produced and evaluated in the same manner as in Example 1. The results are also shown in Table 6.
- polyacrylic acid manufactured by ACROS, product number “185012500”, average molecular weight 240,000
- an electricity storage device lithium ion secondary battery including an electrode made of the binder composition for an electricity storage device according to Comparative Examples 1 to 10 has a poor evaluation of capacity retention rate and voltage drop at high temperature. found. This is presumed that when the amount of iron powder added is 1,000 pieces / mL or less, the electron conductivity in the electrode is poor and the cycle characteristics are adversely affected. Moreover, when it exceeds 100,000 pieces / mL, the iron powder deposited on the negative electrode active material breaks through the separator and short-circuits with the positive electrode, so that it is estimated that the cycle characteristics and the voltage drop during high-temperature storage increase. .
- the present invention is not limited to the above embodiment, and various modifications can be made.
- the present invention includes configurations that are substantially the same as the configurations described in the embodiments (for example, configurations that have the same functions, methods, and results, or configurations that have the same objects and effects).
- the present invention also includes a configuration in which a non-essential part of the configuration described in the above embodiment is replaced with another configuration.
- the present invention includes a configuration that achieves the same effects as the configuration described in the above embodiment or a configuration that can achieve the same object.
- the present invention includes a configuration obtained by adding a known technique to the configuration described in the above embodiment.
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Abstract
Description
本発明に係る蓄電デバイス用バインダー組成物の一態様は、
重合体(A)と、液状媒体(B)と、を含有する蓄電デバイス用バインダー組成物であって、前記組成物中に粒子径10~50μmの粒子が1,000~100,000個/mL含有されていることを特徴とする。
適用例1の蓄電デバイス用バインダー組成物において、
前記重合体(A)が、不飽和カルボン酸エステルに由来する繰り返し単位(Mb)を有することができる。
適用例1または適用例2の蓄電デバイス用バインダー組成物において、
前記重合体(A)が、含フッ素エチレン系単量体に由来する繰り返し単位(Ma)を有する含フッ素系重合体であることができる。
適用例1または適用例2の蓄電デバイス用バインダー組成物において、
前記重合体(A)が、
共役ジエン化合物に由来する繰り返し単位(Md)と、
芳香族ビニルに由来する繰り返し単位(Me)と、
不飽和カルボン酸に由来する繰り返し単位(Mc)と、
を有するジエン系重合体であることができる。
適用例3または適用例4の蓄電デバイス用バインダー組成物において、
前記含フッ素系重合体または前記ジエン系重合体が平均粒子径50~400nmの粒子であり、当該粒子が液状媒体(B)中に分散されていることができる。
本発明に係る蓄電デバイス用電極の製造方法の一態様は、
重合体(A)と、液状媒体(B)と、粒子径10~50μm粒子を1,000~100,000個/mLと、電極活物質とを含有する電極用スラリーを準備する工程と、
前記電極用スラリーを集電体表面に塗布する工程と、
前記集電体表面に塗布された電極用スラリーを乾燥する工程と、
を含むことを特徴とする。
適用例6の蓄電デバイス用電極の製造方法において、
前記重合体(A)が、不飽和カルボン酸エステルに由来する繰り返し単位(Mb)を有することができる。
適用例6または適用例7の蓄電デバイス用電極の製造方法において、
前記重合体(A)が、含フッ素エチレン系単量体に由来する繰り返し単位(Ma)を有する含フッ素系重合体であることができる。
適用例6または適用例7の蓄電デバイス用電極の製造方法において、
前記重合体(A)が、
共役ジエン化合物に由来する繰り返し単位(Md)と、
芳香族ビニルに由来する繰り返し単位(Me)と、
不飽和カルボン酸に由来する繰り返し単位(Mc)と、
を有するジエン系重合体であることができる。
適用例8または適用例9の蓄電デバイス用電極の製造方法において、
前記含フッ素系重合体または前記ジエン系重合体が平均粒子径50~400μmの粒子であって、当該粒子が液状媒体(B)中に分散されていることができる。
本実施の形態に係る蓄電デバイス用バインダー組成物は、重合体(A)と、液状媒体(B)と、を含有し、前記組成物中に粒子径10~50μmの粒子が1,000~100,000個/mL含有されていることを特徴とする。また、前記重合体(A)は、電極活物質層の密着性を良好にするために、不飽和カルボン酸エステルに由来する繰り返し単位(Mb)を有することが好ましい。以下、本実施の形態に係る蓄電デバイス用バインダー組成物に含まれる各成分について詳細に説明する。
本実施の形態に係る蓄電デバイス用バインダー組成物に含まれる重合体(A)は、液状媒体(B)中に溶解していてもよく、粒子として分散されたラテックス状であってもよいが、ラテックス状であることが好ましい。蓄電デバイス用バインダー組成物がラテックス状であると、電極活物質と混合して作製される電極用スラリーの安定性が良好となり、また電極用スラリーの集電体への塗布性が良好となるため好ましい。以下、液状媒体(B)中に粒子として分散された重合体(A)のことを「重合体粒子(A)」ともいう。
本実施の形態で使用される重合体(A)は、不飽和カルボン酸エステルに由来する繰り返し単位(Mb)を有することが好ましい。一般的に、不飽和カルボン酸エステルに由来する繰り返し単位(Mb)を有する重合体は、密着性が良好である。
本実施の形態に係る蓄電デバイス用バインダー組成物が正極を作製するために用いられる場合、重合体(A)は、含フッ素エチレン系単量体に由来する繰り返し単位(Ma)を有する含フッ素系重合体であることが好ましい。
上述したように、本実施の形態で使用することのできる含フッ素系重合体は、含フッ素エチレン系単量体に由来する繰り返し単位(Ma)を有する。含フッ素エチレン系単量体としては、例えばフッ素原子を有するオレフィン化合物、フッ素原子を有する(メタ)アクリレート等が挙げられる。フッ素原子を有するオレフィン化合物としては、例えばフッ化ビニリデン、四フッ化エチレン、六フッ化プロピレン、三フッ化塩化エチレン、パーフルオロアルキルビニルエーテル等が挙げられる。フッ素原子を有する(メタ)アクリレートとしては、例えば下記一般式(1)で表される化合物、(メタ)アクリル酸3[4〔1-トリフルオロメチル-2,2-ビス〔ビス(トリフルオロメチル)フルオロメチル〕エチニルオキシ〕ベンゾオキシ]2-ヒドロキシプロピル等が挙げられる。
重合体(Aa)が四フッ化エチレンに由来する繰り返し単位を含有する場合、その含有割合は、好ましくは1~50質量%であり、より好ましくは2~20質量%である。重合体(Aa)が六フッ化プロピレンに由来する繰り返し単位を含有する場合、その含有割合は、好ましくは1~50質量%であり、より好ましくは2~20質量%である。
上述したように、本実施の形態で使用される含フッ素系重合体は、不飽和カルボン酸エステルに由来する繰り返し単位(Mb)を有することが好ましい。一般的に、不飽和カルボン酸エステルに由来する繰り返し単位(Mb)を有する重合体は、密着性は良好であるが、耐酸化性が不良である場合があった。しかしながら、含フッ素エチレン系単量体に由来する繰り返し単位(Ma)と、不飽和カルボン酸エステルに由来する繰り返し単位(Mb)とを併用することにより、良好な密着性を維持しつつ、より良好な耐酸化性を発現することができる場合がある。
含フッ素系重合体が不飽和カルボン酸に由来する繰り返し単位(Mc)を有することにより、本実施形態の蓄電デバイス用バインダー組成物を用いた電極用スラリーの安定性が向上する。
含フッ素系重合体は、上記以外の繰り返し単位を有してもよい。上記以外の繰り返し単位としては、例えばα,β-不飽和ニトリル化合物、共役ジエン化合物、芳香族ビニルおよびその他の不飽和単量体を挙げることができる。
含フッ素系重合体は、上記のような構成を採るものである限り、その合成方法は特に限定されないが、例えば公知の乳化重合工程またはこれを適宜に組み合わせることによって、容易に合成することができる。たとえば、特許4957932号公報に記載の方法等を用いることにより容易に合成することができる。
本実施の形態に係る蓄電デバイス用バインダー組成物が負極を作製するために用いられる場合、重合体(A)はジエン系重合体であることが好ましい。ジエン系重合体は、共役ジエン化合物に由来する繰り返し単位(Md)と、芳香族ビニルに由来する繰り返し単位(Me)と、不飽和カルボン酸エステルに由来する繰り返し単位(Mb)と、不飽和カルボン酸に由来する繰り返し単位(Mc)と、を有することが好ましい。
ジエン系重合体が共役ジエン化合物に由来する繰り返し単位(Md)を有することにより、粘弾性及び強度に優れた負極用バインダー組成物を製造することが容易となる。すなわち、共役ジエン化合物に由来する繰り返し単位を有する重合体を使用すると、重合体が強い結着力を有することができる。共役ジエン化合物に由来するゴム弾性が重合体に付与されるため、電極の体積収縮や拡大等の変化に追従することが可能となる。これにより、結着性を向上させると考えられる。
ジエン系重合体が芳香族ビニルに由来する繰り返し単位(Me)を有することにより、負極用スラリーが導電付与剤を含有する場合に、これに対する親和性をより良好にすることができる。
ジエン系重合体が不飽和カルボン酸エステルに由来する繰り返し単位(Mb)を有することにより、電解液との親和性がより良好となり、蓄電デバイス中でバインダーが電気抵抗成分となることによる内部抵抗の上昇を抑制するとともに、電解液を過大に吸収することによる結着性の低下をより効果的に防ぐことができる。
ジエン系重合体が不飽和カルボン酸に由来する繰り返し単位(Mc)を有することにより、本実施形態の蓄電デバイス用バインダー組成物を用いた電極用スラリーの安定性が向上する。
ジエン系重合体は、上記以外の繰り返し単位を有してもよい。上記以外の繰り返し単位としては、例えばα,β-不飽和ニトリル化合物に由来する繰り返し単位が挙げられる。
ジエン系重合体、上記のような構成を採るものである限り、その合成方法は特に限定されないが、例えば公知の乳化重合工程またはこれを適宜に組み合わせることによって、容易に合成することができる。たとえば、特許4957932号公報に記載の方法等を用いることにより容易に合成することができる。
1.1.4.1.テトラヒドロフラン(THF)不溶分
重合体(A)のTHF不溶分は、80%以上であることが好ましく、90%以上であることがより好ましい。THF不溶分は、蓄電デバイスで使用する電解液への不溶分量とほぼ比例すると推測される。このため、THF不溶分が前記範囲であれば、蓄電デバイスを作製して、長期間にわたり充放電を繰り返した場合でも電解液への重合体(A)の溶出を抑制できるため良好であると推測できる。
重合体(A)が含フッ素系重合体である場合、JIS K7121に準拠する示差走査熱量測定(DSC)によって測定したときに、-50~250℃の温度範囲において吸熱ピークを1つしか有さないものであることが好ましい。この吸熱ピークの温度は、-30~+30℃の範囲にあることがより好ましい。重合体(Aa)が単独で存在する場合には、一般的に-50~250℃に吸熱ピーク(融解温度)を有することが好ましい。
本実施の形態に係る蓄電デバイス用バインダー組成物に含まれる重合体(A)が、液状媒体(B)中に粒子として分散されたラテックス状である場合、重合体粒子(A)の平均粒子径は、50~400nmの範囲にあることが好ましく、100~250nmの範囲にあることがより好ましい。重合体粒子(A)の平均粒子径が前記範囲にあると、電極活物質の表面に重合体粒子(A)が十分に吸着することができるため、電極活物質の移動に伴って重合体粒子(A)も追従して移動することができる。その結果、両者の粒子のうちのどちらかのみが単独でマイグレーションすることを抑制することができるので、電気的特性の劣化を抑制することができる。
本実施の形態に係る蓄電デバイス用バインダー組成物は、液状媒体(B)を含有する。液状媒体(B)としては、水を含有する水系媒体であることが好ましい。上記水系媒体には、水以外の非水系媒体を含有させることができる。この非水系媒体としては、例えばアミド化合物、炭化水素、アルコール、ケトン、エステル、アミン化合物、ラクトン、スルホキシド、スルホン化合物などを挙げることができ、これらのうちから選択される1種以上を使用することができる。液状媒体(B)が、水と、水以外の非水系媒体とを含有する場合、液状媒体(B)の全量100質量%中、90質量%以上が水であることが好ましく、98質量%以上が水であることがさらに好ましい。本実施の形態に係る蓄電デバイス用バインダー組成物は、液状媒体(B)として水系媒体を使用することにより、環境に対して悪影響を及ぼす程度が低くなり、取扱作業者に対する安全性も高くなる。
本実施の形態に係る蓄電デバイス用バインダー組成物は、必要に応じて前述した重合体(A)、液状媒体(B)以外の添加剤を含有することができる。このような添加剤としては、例えば、防腐剤や増粘剤が挙げられる。本実施の形態に係る蓄電デバイス用バインダー組成物は、防腐剤を含有することにより貯蔵安定性がより向上し、また増粘剤を含有することにより、その塗布性や得られる蓄電デバイスの充放電特性等をさらに向上させることができる。
本実施の形態に係る蓄電デバイス用バインダー組成物は、防腐剤を含有することができる。特に、蓄電デバイス用バインダー組成物に防腐剤としてイソチアゾリン系化合物を添加することにより、蓄電デバイス用バインダー組成物を貯蔵した際に、細菌や黴などが増殖して異物が発生することを抑制することができる。さらに、蓄電デバイスの充放電時にバインダーの劣化が抑制されるため、蓄電デバイスの充放電特性の低下を抑制することができる。
増粘剤としては、例えば、カルボキシメチルセルロース、メチルセルロース、ヒドロキシプロピルセルロースなどのセルロース化合物;上記セルロース化合物のアンモニウム塩またはアルカリ金属塩;ポリ(メタ)アクリル酸、変性ポリ(メタ)アクリル酸などのポリカルボン酸;上記ポリカルボン酸のアルカリ金属塩;ポリビニルアルコール、変性ポリビニルアルコール、エチレン-ビニルアルコール共重合体などのポリビニルアルコール系(共)重合体;(メタ)アクリル酸、マレイン酸およびフマル酸などの不飽和カルボン酸とビニルエステルとの共重合体の鹸化物などの水溶性ポリマーなどを挙げることができる。これらの中でも特に好ましい増粘剤としては、カルボキシメチルセルロースのアルカリ金属塩、ポリ(メタ)アクリル酸およびそのアルカリ金属塩である。
本実施の形態に係る蓄電デバイス用バインダー組成物は、組成物中に粒子径が10~50μmの粒子を含有する。
上述の蓄電デバイス用バインダー組成物を用いて電極用スラリーを製造することができる。電極用スラリーとは、これを集電体の表面に塗布した後、乾燥して、集電体表面上に電極活物質層を形成するために用いられる分散液のことをいう。本実施の形態に係る電極用スラリーは、上述の蓄電デバイス用バインダー組成物と、電極活物質とを含有する。以下、本実施の形態に係る電極用スラリーに含まれる成分についてそれぞれ詳細に説明する。ただし、蓄電デバイス用バインダー組成物については、前述した通りであるから説明を省略する。
本実施の形態に係る電極用スラリーに含まれる電極活物質を構成する材料としては特に制限はなく、目的とする蓄電デバイスの種類により適宜適当な材料を選択することができる。
Li1+xM1 yM2 zO4 ・・・・・(3b)
(式(3a)および(3b)中、M1はCo、NiおよびMnよりなる群から選択される少なくとも1種の金属原子であり;M2はAlおよびSnよりなる群から選択される少なくとも1種の金属原子であり;Oは酸素原子であり;x、yおよびzは、それぞれ、0.10≧x≧0、4.00≧y≧0.85および2.00≧z≧0の範囲の数である。)
Li1-xM3 x(XO4) ・・・・・(4)
(式(4)中、M3は、Mg、Ti、V、Nb、Ta、Cr、Mn、Fe、Co、Ni、Cu、Zn、Al、Ga、GeおよびSnよりなる群から選択される金属のイオンの少なくとも1種であり;Xは、Si、S、PおよびVよりなる群から選択される少なくとも1種であり;xは数であり、0<x<1の関係を満たす。)
なお、上記一般式(4)におけるxの値は、M3およびXの価数に応じて、それぞれ上記一般式(4)全体の価数が0価となるように選択される。
上記電極用スラリーは、必要に応じて前述した成分以外の成分を含有することができる。このような成分としては、例えば導電付与剤、水、非水系媒体、増粘剤等が挙げられる。
上記導電付与剤の具体例としては、リチウムイオン二次電池においてはカーボンなどが;ニッケル水素二次電池においては、正極では酸化コバルトが:負極ではニッケル粉末、酸化コバルト、酸化チタン、カーボンなどが、それぞれ用いられる。上記両電池において、カーボンとしては、グラファイト、活性炭、アセチレンブラック、ファーネスブラック、黒鉛、炭素繊維、フラーレンなどを挙げることができる。これらの中でも、アセチレンブラックまたはファーネスブラックを好ましく使用することができる。導電付与剤の使用割合は、電極活物質100質量部に対して、好ましくは20質量部以下であり、より好ましくは1~15質量部であり、特に好ましくは2~10質量部である。
上記電極用スラリーは、その塗布性を改善する観点から、80~350℃の標準沸点を有する非水系媒体を含有することができる。このような非水系媒体の具体例としては、例えばN-メチルピロリドン、ジメチルホルムアミド、N,N-ジメチルアセトアミドなどのアミド化合物;トルエン、キシレン、n-ドデカン、テトラリンなどの炭化水素;2-エチル-1-ヘキサノール、1-ノナノール、ラウリルアルコールなどのアルコール;メチルエチルケトン、シクロヘキサノン、ホロン、アセトフェノン、イソホロンなどのケトン;酢酸ベンジル、酪酸イソペンチル、乳酸メチル、乳酸エチル、乳酸ブチルなどのエステル;o-トルイジン、m-トルイジン、p-トルイジンなどのアミン化合物;γ-ブチロラクトン、δ-ブチロラクトンなどのラクトン;ジメチルスルホキシド、スルホランなどのスルホキシド・スルホン化合物などを挙げることができ、これらのうちから選択される1種以上を使用することができる。これらの中でも、重合体粒子の安定性、電極用スラリーを塗布する際の作業性などの点から、N-メチルピロリドンを使用することが好ましい。
上記電極用スラリーは、その塗工性を改善する観点から、増粘剤を含有することができる。増粘剤の具体例としては、上記「1.3.2.増粘剤」に記載した各種化合物が挙げられる。
本実施の形態に係る電極用スラリーは、前述の蓄電デバイス用バインダー組成物と、電極活物質と、必要に応じて用いられる添加剤と、を混合することにより製造することができる。これらの混合は公知の手法による攪拌によって行うことができ、例えば攪拌機、脱泡機、ビーズミル、高圧ホモジナイザーなどを利用することができる。
本実施の形態に係る電極は、集電体と、前記集電体の表面上に前述の電極用スラリーが塗布および乾燥されて形成された層と、を備えるものである。かかる電極は、金属箔などの適宜の集電体の表面に、上述の電極用スラリーを塗布して塗膜を形成し、次いで該塗膜を乾燥して電極活物質層を形成することにより製造することができる。このようにして製造された電極は、集電体上に、前述の重合体(A)、粒子径が10~50μmの粒子および電極活物質、さらに必要に応じて添加した任意成分を含有する電極活物質層が結着されてなるものである。かかる電極は、集電体と電極活物質層との結着性に優れるとともに、電気的特性の一つである充放電レート特性が良好である。したがって、このような電極は蓄電デバイスの電極として好適である。
本実施の形態に係る蓄電デバイスは、上述の電極を備えるものであり、さらに電解液を含有し、セパレータなどの部品を用いて、常法に従って製造することができる。具体的な製造方法としては、例えば、負極と正極とをセパレータを介して重ね合わせ、これを電池形状に応じて巻く、折るなどして電池容器に入れ、電池容器に電解液を注入して封口する方法が挙げられる。電池の形状は、コイン型、ボタン型、シート型、円筒型、角形、扁平型など、適宜の形状であることができる。
以下、本発明を実施例に基づいて具体的に説明するが、本発明はこれらの実施例に限定されるものではない。実施例、比較例中の「部」および「%」は、特に断らない限り質量基準である。
5.1.1.重合体(A)の作製
電磁式撹拌機を備えた内容積約6Lのオートクレーブの内部を十分に窒素置換した後、脱酸素した純水2.5Lおよび乳化剤としてパーフルオロデカン酸アンモニウム25gを仕込み、350rpmで撹拌しながら60℃まで昇温した。次いで、単量体であるフッ化ビニリデン(VDF)70%および六フッ化プロピレン(HFP)30%からなる混合ガスを、内圧が20kg/cm2に達するまで仕込んだ。重合開始剤としてジイソプロピルパーオキシジカーボネートを20%含有するフロン113溶液25gを窒素ガスを使用して圧入し、重合を開始した。重合中は内圧が20kg/cm2に維持されるようVDF60.2%およびHFP39.8%からなる混合ガスを逐次圧入して、圧力を20kg/cm2に維持した。また、重合が進行するに従って重合速度が低下するため、3時間経過後に、先と同じ重合開始剤溶液の同量を窒素ガスを使用して圧入し、さらに3時間反応を継続した。その後、反応液を冷却すると同時に撹拌を停止し、未反応の単量体を放出した後に反応を停止することにより、重合体(Aa)の微粒子を40%含有する水系分散体を得た。得られた重合体(Aa)につき、19F-NMRにより分析した結果、各単量体の質量組成比はVDF/HFP=21/4であった。
さらに、得られた微粒子を示差走査熱量計(DSC)によって測定したところ、単一のガラス転移温度Tgが-5℃に一つだけ観測された。2種類の重合体を用いているにもかかわらず、得られた重合体粒子(A)は一つのTgしか示さないため、重合体(A)はポリマーアロイであると推測できる。
上記で得られた重合体粒子(A)を含有する水系分散体1,000gに、2-メチル-4-イソチアゾリン-3-オンを1%含有する水懸濁液を31g仕込み、300rpmで撹拌することにより、重合体組成物F1の調製を行った。なお、以下の合成例において、防腐剤が水不溶性の場合、超音波により水溶液に分散させた状態の分散液を添加して重合体組成物の調製を行った。
上記合成例1の「5.1.1.重合体(A)の作製」において、単量体の組成と乳化剤量を適宜に変更したほかは合成例1と同様にして、表1に示す組成の重合体(A)を含有する水系分散体を調製し、該水系分散体の固形分濃度に応じて水を減圧除去または追加することにより、固形分濃度40%の水系分散体を得た。なお、合成例2~7および合成例11で得られた微粒子を示差走査熱量計(DSC)によって測定したところ、単一のガラス転移温度Tgが表1に記載の温度で一つだけ観測された。2種類の重合体を用いているにもかかわらず、得られた重合体(A)は一つのTgしか示さないため、重合体(A)はポリマーアロイであると推測できる。
容量7リットルのセパラブルフラスコに、水150質量部およびドデシルベンゼンスルホン酸ナトリウム0.2質量部を仕込み、セパラブルフラスコの内部を十分に窒素置換した。一方、別の容器に、水60質量部、乳化剤としてエーテルサルフェート型乳化剤(商品名「アデカリアソープSR1025」、株式会社ADEKA製)を固形分換算で0.8質量部ならびに単量体として2,2,2-トリフルオロエチルメタクリレート(TFEMA)20質量部、アクリロニトリル(AN)10質量部、メチルメタクリレート(MMA)25質量部、2-エチルヘキシルアクリレート(EHA)40質量部およびアクリル酸(AA)5質量部を加え、十分に攪拌して上記単量体の混合物を含有する単量体乳化液を調製した。その後、上記セパラブルフラスコの内部の昇温を開始し、当該セパラブルフラスコの内部の温度が60℃に到達した時点で、重合開始剤として過硫酸アンモニウム0.5質量部を加えた。そして、セパラブルフラスコの内部の温度が70℃に到達した時点で、上記で調製した単量体乳化液の添加を開始し、セパラブルフラスコの内部の温度を70℃に維持したまま単量体乳化液を3時間かけてゆっくりと添加した。その後、セパラブルフラスコの内部の温度を85℃に昇温し、この温度を3時間維持して重合反応を行った。3時間後、セパラブルフラスコを冷却して反応を停止した後、アンモニウム水を加えてpHを7.6に調整することにより、重合体粒子(A)を30%含有する水系分散体を得た。
各単量体の種類及び仕込み量(部)をそれぞれ表1の通りとしたほかは上記合成例8と同様にして、表1に記載の重合体(A)を含有する水系分散体をそれぞれ得た。このようにして得られた水系分散体を使用したこと以外は、合成例1と同様にして重合体組成物F9~F10を作製した。
・VDF:フッ化ビニリデン
・HFP:六フッ化プロピレン
・TFEMA:メタクリル酸2,2,2-トリフルオロエチル
・TFEA:アクリル酸2,2,2-トリフルオロエチル
・HFIPA:アクリル酸1,1,1,3,3,3-ヘキサフルオロイソプロピル
・MMA:メタクリル酸メチル
・EHA:アクリル酸2-エチルヘキシル
・MAA:メタクリル酸
・AA :アクリル酸
・DVB:ジビニルベンゼン
・TMPTMA:トリメタクリル酸トリメチロールプロパン
・AN :アクリロニトリル
攪拌機を備えた温度調節可能なオートクレーブ中に、水200質量部、ドデシルベンゼンスルホン酸ナトリウム0.9質量部、過硫酸カリウム1.0質量部、重亜硫酸ナトリウム0.5質量部、α-メチルスチレンダイマー0.2質量部、ドデシルメルカプタン0.2質量部、および表3に示した一段目重合成分を一括して仕込み、70℃に昇温し2時間重合反応させた。重合添加率が80%以上であることを確認した後、反応温度を70℃に維持したまま、表3に示す二段目重合成分を6時間かけて添加した。二段目重合成分添加開始から3時間経過した時点で、α-メチルスチレンダイマー1.0質量部およびドデシルメルカプタン0.3質量部を添加した。二段目重合成分添加終了後、温度を80℃に昇温し、さらに2時間反応させた。重合反応終了後、ラテックスのpHを7.5に調節し、トリポリリン酸ナトリウム5質量部(固形分換算)を添加した。その後、残留モノマーを水蒸気蒸留で処理し、減圧下で固形分50%まで濃縮することで、重合体(A)を50%含有する水系分散体を得た。
各単量体の種類および仕込み量(部)をそれぞれ表2の通りとし、重合体(A)を作製する際の、一段目重合成分および二段目重合成分の含有割合を表3の通りとした他は上記合成例12と同様にして、表2に記載の重合体(A)を含有する水系分散体をそれぞれ得た。このようにして得られた水系分散体を使用したこと以外は、合成例1と同様にして重合体組成物S2~S13を作製した。
・MMA:メタクリル酸メチル
・HEMA:メタクリル酸2-ヒドロキシエチル
・AA :アクリル酸
・TA :イタコン酸
・AN :アクリロニトリル
・BD :1,3-ブタジエン
・ST :スチレン
電磁式撹拌機を備えた内容積約6リットルのオートクレーブの内部を十分に窒素置換した後、脱酸素した純水2.5リットル、及び乳化剤としてパーフルオロデカン酸アンモニウム25gを仕込み、350rpmで撹拌しながら60℃まで昇温した。次いで、フッ化ビニリデン(VDF)44.2%、及び六フッ化プロピレン(HFP)55.8%からなる混合ガスを、内圧が20kg/cm2Gに達するまで仕込んだ。その後、重合開始剤としてジイソプロピルパーオキシジカーボネートを20%含有するフロン113溶液25gを、窒素ガスを使用して圧入し、重合を開始させた。重合中はVDF60.2%、及びHFP39.8%からなる混合ガスを逐次圧入して、圧力を20kg/cm2Gに維持した。また、重合の進行とともに重合速度が低下するため、3時間経過後に、先と同量の重合開始剤を、窒素ガスを使用して圧入して、更に3時間反応を継続させた。反応液を冷却するとともに撹拌を停止し、未反応単量体を放出して反応を停止させ、フッ素重合体のラテックスを得た。
各単量体の種類及び仕込み量(質量部)をそれぞれ表4の通りとし、重合体(A)を作製する際の、一段目重合成分および二段目重合成分の含有割合を表4の通りとした以外は上記合成例25と同様にして、表4に記載の重合体(A)を含有するNMP溶液をそれぞれ得た。このようにして得られたNMP溶液を使用したこと以外は、合成例25と同様にして重合体組成物F13~F17を作製した。
・VDF:フッ化ビニリデン
・HFP:六フッ化プロピレン
・nBA:n-ブチルアクリレート
・MMA:メチルメタクリレート
・ST:スチレン
・IA:イタコン酸
・ATBS:2-アクリルアミド-2-メチルプロパンスルホン酸
・NMAM:N-メチロールアクリルアミド
・NASS:スチレンスルホン酸ナトリウム
・GMA:グリシジルメタクリレート
5.9.1.蓄電デバイス用バインダー組成物の作製
前記「5.1.2.重合体組成物の調製」で作製した重合体組成物F1へ、あらかじめふるいにより分級しておいた20μm以下の鉄粉を添加して、撹拌した。このようにして作製した混合物をマグネットフィルター(磁力:1.7T、流量15kg/min)を通過させ、粗大な鉄粉を除去した。得られた蓄電デバイス用バインダー組成物について、顕微鏡にて鉄粉の粒径並びに個数を確認した。
二軸型プラネタリーミキサー(プライミクス株式会社製、商品名「TKハイビスミックス 2P-03」)に増粘剤(商品名「CMC1120」、株式会社ダイセル製)1質量部(固形分換算)、市販のリン酸鉄リチウム(LiFePO4)をめのう乳鉢で粉砕し、ふるいを用いて分級することにより得られた粒子径(D50値)が0.5μmである電極活物質100質量部、アセチレンブラック5質量部および水68質量部を投入し、60rpmで1時間攪拌を行った。次いで、上記「5.9.1.蓄電デバイス用バインダー組成物の作製」で得られた蓄電デバイス用バインダー組成物を、該組成物中に含有される重合体粒子が1質量部となるように加え、さらに1時間攪拌してペーストを得た。得られたペーストに水を加えて固形分濃度を50%に調整した後、攪拌脱泡機(株式会社シンキー製、商品名「あわとり練太郎」)を使用して、200rpmで2分間、1,800rpmで5分間、さらに真空下(約5.0×103Pa)において1,800rpmで1.5分間攪拌混合することにより、電極用スラリーを調製した。
厚み30μmのアルミニウム箔からなる集電体の表面に、上記「5.9.2.電極用スラリーの調製」で調製した電極用スラリーを、乾燥後の膜厚が100μmとなるようにドクターブレード法によって均一に塗布し、120℃で20分間乾燥した。その後、膜(電極活物質層)の密度が1.9g/cm3になるようにロールプレス機によりプレス加工することにより、蓄電デバイス用電極(正極)を得た。
<対極(負極)の製造>
二軸型プラネタリーミキサー(プライミクス株式会社製、商品名「TKハイビスミックス 2P-03」)に、ポリフッ化ビニリデン(PVDF)4質量部(固形分換算)、負極活物質としてグラファイト100質量部(固形分換算)、N-メチルピロリドン(NMP)80質量部を投入し、60rpmで1時間撹拌を行った。その後、さらにNMP20質量部を投入した後、撹拌脱泡機(株式会社シンキー製、製品名「あわとり練太郎」)を使用して、200rpmで2分間、次いで1,800rpmで5分間、さらに真空下において1,800rpmで1.5分間撹拌・混合することにより、対極(負極)用スラリーを調製した。
露点が-80℃以下となるようAr置換されたグローブボックス内で、上記で製造した電極(負極)を直径15.95mmに打ち抜き成形したものを、2極式コインセル(宝泉株式会社製、商品名「HSフラットセル」)上に載置した。次いで、直径24mmに打ち抜いたポリプロピレン製多孔膜からなるセパレータ(セルガード株式会社製、商品名「セルガード#2400」)を載置し、さらに、空気が入らないように電解液を500μL注入した後、上記で製造した正極を直径16.16mmに打ち抜き成形したものを載置し、前記2極式コインセルの外装ボディーをネジで閉めて封止することにより、リチウムイオン電池セル(蓄電デバイス)を組み立てた。ここで使用した電解液は、エチレンカーボネート/エチルメチルカーボネート=1/1(質量比)の溶媒に、LiPF6を1モル/Lの濃度で溶解した溶液である。
上記で作製したリチウムイオン二次電池を、定電流(1C)にて充電を開始し、電圧が4.2Vになった時点で引き続き定電圧(4.2V)にて充電を続行し、電流値が0.01Cとなった時点を充電完了(カットオフ)とした。その後、定電流(1C)にて放電を開始し、電圧が3.0Vになった時点を放電完了(カットオフ)とし、1サイクル目の放電容量を算出した。このようにして50回充放電を繰り返し、50サイクル目の放電容量を算出した。このようにして測定した50サイクル目の放電容量を、1サイクル目の放電容量で割った値を放電容量維持率(%)として、表5に併せて示した。放電容量維持率が80%以上である場合、良好と判断できる。
上記で作製したリチウムイオン二次電池を、25℃で定電流(1C)にて充電を開始し、電圧が4.2Vになった時点で引き続き定電圧(4.2V)にて充電を続行し、電流値が0.01Cとなった時点を充電完了とした。その電池の電池電圧を測定後に絶縁性の仕切りのある容器(この実施例ではPP製の容器)に入れたものを60℃の恒温槽に投入して、2週間保存した。その後、取出して25℃の恒温槽に静置して3h後に電池電圧を測定した。保存前後の電圧差(=高温保存前電池電圧-高温保存後電池電圧)を測定し、高温時の電圧低下(mV)の評価を行った。測定された高温時の電圧低下(mV)の値を、表5に併せて示した。電圧低下が50mV以下である場合、良好と判断できる。
実施例1の「5.9.1.蓄電デバイス用バインダー組成物の作製」において、表5に示す重合体組成物と条件とした以外は、実施例1と同様にして蓄電デバイス用バインダー組成物、蓄電デバイス用電極及び蓄電デバイスを作製し、評価した。その結果を表5に併せて示した。なお、SUS粉(SUS430)についても実施例1と同様に、あらかじめふるいにより分級しておいた20μm以下のSUS粉を添加し、マグネットフィルターを通過させ粗大SUS粒を除去して実施した。
5.11.1.蓄電デバイス用バインダー組成物の作製
表6に示す組成物と条件とした以外は、実施例1と同様にして蓄電デバイス用バインダー組成物を作製した。
二軸型プラネタリーミキサー(プライミクス株式会社製、商品名「TKハイビスミックス 2P-03」)に増粘剤(商品名「CMC2200」、株式会社ダイセル製)1質量部(固形分換算)、負極活物質としてグラファイト100質量部(固形分換算)、水68質量部を投入し、60rpmで1時間攪拌を行った。その後、上記「5.11.1.蓄電デバイス用バインダー組成物」で作製した蓄電デバイス用バインダー組成物2質量部(固形分換算)を加え、さらに1時間攪拌しペーストを得た。得られたペーストに水を投入し、固形分を50%に調製した後、攪拌脱泡機(株式会社シンキー製、商品名「泡とり練太郎」)を使用して、200rpmで2分間、1800rpmで5分間、さらに真空下において1800rpmで1.5分間攪拌混合することにより、電極用スラリーを調製した。
厚み20μmの銅箔よりなる集電体の表面に、上記「5.11.2.電極用スラリーの調製」で調製した電極用スラリーを、乾燥後の膜厚が80μmとなるようにドクターブレード法によって均一に塗布し、120℃で20分間乾燥処理した。その後、電極層の密度が1.5g/cm3になるようにロールプレス機によりプレス加工することにより、電極(負極)を得た。
<対極(正極)の製造>
二軸型プラネタリーミキサー(プライミクス株式会社製、商品名「TKハイビスミックス 2P-03」)に電気化学デバイス電極用バインダー(株式会社クレハ製、商品名「KFポリマー#1120」)4.0質量部(固形分換算)、導電助剤(電気化学工業株式会社製、商品名「デンカブラック50%プレス品」)3.0質量部、正極活物質として粒径5μmのLiCoO2(ハヤシ化成株式会社製)100質量部(固形分換算)、N-メチルピロリドン(NMP)36質量部を投入し、60rpmで2時間攪拌を行った。得られたペーストにNMPを投入し、固形分を65%に調製した後、攪拌脱泡機(株式会社シンキー製、商品名「泡とり練太郎」)を使用して、200rpmで2分間、1800rpmで5分間、さらに真空下において1800rpmで1.5分間攪拌混合することにより、電極用スラリーを調製した。アルミニウム箔よりなる集電体の表面に、調製した電極用スラリーを、乾燥後の膜厚が80μmとなるようにドクターブレード法によって均一に塗布し、120℃で20分間乾燥処理した。その後、電極層の密度が3.0g/cm3となるようにロールプレス機によりプレス加工することにより、対極(正極)を得た。
露点が-80℃以下となるようAr置換されたグローブボックス内で、上記で製造した電極(負極)を直径15.95mmに打ち抜き成型したものを、2極式コインセル(宝泉株式会社製、商品名「HSフラットセル」)上に載置した。次いで、直径24mmに打ち抜いたポリプロピレン製多孔膜からなるセパレータ(セルガード株式会社製、商品名「セルガード#2400」)を載置し、さらに、空気が入らないように電解液を500μL注入した後、上記で製造した正極を直径16.16mmに打ち抜き成型したものを載置し、前記2極式コインセルの外装ボディーをネジで閉めて封止することにより、リチウムイオン電池セル(蓄電デバイス)を組み立てた。ここで使用した電解液は、エチレンカーボネート/エチルメチルカーボネート=1/1(質量比)の溶媒に、LiPF6を1モル/Lの濃度で溶解した溶液である。
実施例1の「5.9.4.蓄電デバイスの製造及び評価」の<容量維持率の評価>及び<高温時の電圧低下の評価>の項に記載の方法により、容量維持率及び高温時電圧低下を評価した。結果を表6に併せて示す。
実施例1の「5.9.1.蓄電デバイス用バインダー組成物の作製」において、表6に示す重合体組成物及び条件とした以外は、実施例1と同様にして蓄電デバイス用バインダー組成物、蓄電デバイス用電極及び蓄電デバイスを作製し、評価した。その結果を表6に併せて示した。
上記表4と表5から明らかなように、実施例1~54に示した本発明に係る蓄電デバイス用バインダー組成物を用いて作製された蓄電デバイス(リチウムイオン二次電池)は、良好な容量維持率を示した。これは、添加された粒子(鉄粉やSUS粉)が電極内に均一に分散することにより、電極内の電子伝導性が向上したためと推測される。さらに高温保存時の電圧低下は問題ない結果が得られた。
Claims (10)
- 重合体(A)と、液状媒体(B)と、を含有する蓄電デバイス用バインダー組成物であって、
前記組成物中に粒子径10~50μmの粒子が1,000~100,000個/mL含有されている、蓄電デバイス用バインダー組成物。 - 前記重合体(A)が、不飽和カルボン酸エステルに由来する繰り返し単位(Mb)を有する、請求項1に記載の蓄電デバイス用バインダー組成物。
- 前記重合体(A)が、含フッ素エチレン系単量体に由来する繰り返し単位(Ma)を有する含フッ素系重合体である、請求項1または請求項2に記載の蓄電デバイス用バインダー組成物。
- 前記重合体(A)が、
共役ジエン化合物に由来する繰り返し単位(Md)と、
芳香族ビニルに由来する繰り返し単位(Me)と、
不飽和カルボン酸に由来する繰り返し単位(Mc)と、
を有するジエン系重合体である、請求項1または請求項2に記載の蓄電デバイス用バインダー組成物。 - 前記含フッ素系重合体または前記ジエン系重合体が平均粒子径50~400nmの粒子であり、当該粒子が液状媒体(B)中に分散されている、請求項3または請求項4に記載の蓄電デバイス用バインダー組成物。
- 重合体(A)と、液状媒体(B)と、粒子径10~50μm粒子を1,000~100,000個/mLと、電極活物質とを含有する電極用スラリーを準備する工程と、
前記電極用スラリーを集電体表面に塗布する工程と、
前記集電体表面に塗布された電極用スラリーを乾燥する工程と、
を含む、蓄電デバイス用電極の製造方法。 - 前記重合体(A)が、不飽和カルボン酸エステルに由来する繰り返し単位(Mb)を有する、請求項6に記載の蓄電デバイス用電極の製造方法。
- 前記重合体(A)が、含フッ素エチレン系単量体に由来する繰り返し単位(Ma)を有する含フッ素系重合体である、請求項6または請求項7に記載の蓄電デバイス用電極の製造方法。
- 前記重合体(A)が、
共役ジエン化合物に由来する繰り返し単位(Md)と、
芳香族ビニルに由来する繰り返し単位(Me)と、
不飽和カルボン酸に由来する繰り返し単位(Mc)と、
を有するジエン系重合体である、請求項6または請求項7に記載の蓄電デバイス用電極の製造方法。 - 前記含フッ素系重合体または前記ジエン系重合体が平均粒子径50~400μmの粒子であって、当該粒子が液状媒体(B)中に分散されている、請求項8または請求項9に記載の蓄電デバイス用電極の製造方法。
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2015
- 2015-06-23 US US15/323,452 patent/US10505195B2/en active Active
- 2015-06-23 JP JP2015549700A patent/JP5904350B1/ja active Active
- 2015-06-23 KR KR1020167036817A patent/KR20170026397A/ko not_active Ceased
- 2015-06-23 WO PCT/JP2015/068030 patent/WO2016002586A1/ja not_active Ceased
- 2015-06-23 CN CN201580036033.4A patent/CN106471654A/zh active Pending
- 2015-07-03 TW TW104121685A patent/TWI666816B/zh active
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| WO2016103730A1 (ja) * | 2014-12-26 | 2016-06-30 | 日本ゼオン株式会社 | 非水系二次電池正極用バインダー組成物、非水系二次電池正極用組成物、非水系二次電池用正極および非水系二次電池、並びに、非水系二次電池正極用組成物、非水系二次電池用正極および非水系二次電池の製造方法 |
| JPWO2016103730A1 (ja) * | 2014-12-26 | 2017-10-05 | 日本ゼオン株式会社 | 非水系二次電池正極用バインダー組成物、非水系二次電池正極用組成物、非水系二次電池用正極および非水系二次電池、並びに、非水系二次電池正極用組成物、非水系二次電池用正極および非水系二次電池の製造方法 |
| JP2017188456A (ja) * | 2016-03-31 | 2017-10-12 | 三洋化成工業株式会社 | リチウムイオン電池用被覆正極活物質 |
| JPWO2023182308A1 (ja) * | 2022-03-25 | 2023-09-28 |
Also Published As
| Publication number | Publication date |
|---|---|
| US20170149064A1 (en) | 2017-05-25 |
| JPWO2016002586A1 (ja) | 2017-04-27 |
| CN106471654A (zh) | 2017-03-01 |
| JP5904350B1 (ja) | 2016-04-13 |
| TWI666816B (zh) | 2019-07-21 |
| KR20170026397A (ko) | 2017-03-08 |
| US10505195B2 (en) | 2019-12-10 |
| TW201607128A (zh) | 2016-02-16 |
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