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WO2025205922A1 - Electrode mixture, electrode, and battery - Google Patents

Electrode mixture, electrode, and battery

Info

Publication number
WO2025205922A1
WO2025205922A1 PCT/JP2025/011997 JP2025011997W WO2025205922A1 WO 2025205922 A1 WO2025205922 A1 WO 2025205922A1 JP 2025011997 W JP2025011997 W JP 2025011997W WO 2025205922 A1 WO2025205922 A1 WO 2025205922A1
Authority
WO
WIPO (PCT)
Prior art keywords
vinylidene fluoride
electrode mixture
electrode
active material
fluoride copolymer
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
PCT/JP2025/011997
Other languages
French (fr)
Japanese (ja)
Inventor
宏 佐藤
拓也 山根
颯介 黒川
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kureha Corp
Original Assignee
Kureha Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kureha Corp filed Critical Kureha Corp
Publication of WO2025205922A1 publication Critical patent/WO2025205922A1/en
Pending legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F214/00Copolymers 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 a halogen
    • C08F214/18Monomers containing fluorine
    • C08F214/22Vinylidene fluoride
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F220/00Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
    • C08F220/02Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
    • C08F220/04Acids; Metal salts or ammonium salts thereof
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K9/00Use of pretreated ingredients
    • C08K9/02Ingredients treated with inorganic substances
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L27/00Compositions of 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 a halogen; Compositions of derivatives of such polymers
    • C08L27/02Compositions of 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 a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L27/12Compositions of 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 a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
    • C08L27/16Homopolymers or copolymers or vinylidene fluoride
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/13Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H01M4/139Processes of manufacture
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/58Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Definitions

  • the present invention relates to an electrode mixture, an electrode, and a battery.
  • An electrode mixture containing a binder and active material is typically used to form the mixture layer of an electrode in a non-aqueous electrolyte secondary battery.
  • Vinylidene fluoride polymer is typically used as the binder.
  • High adhesiveness is required for the binder, as it serves the purpose of adhering the active material to the current collector.
  • Patent Document 1 describes introducing functional groups such as carboxyl groups into a fluorine-based resin to improve adhesion to the current collector and solubility in solvents.
  • Patent Document 2 describes a binder composition containing a copolymer of vinylidene fluoride and a compound with a specific structure (vinylidene fluoride copolymer), and describes that the vinylidene fluoride copolymer exhibits high adhesion to the current collector.
  • LFP lithium iron phosphate
  • LFMP lithium iron manganese phosphate
  • the present invention was made in consideration of the above-mentioned problems. It aims to provide an electrode mixture that contains a carbon-coated electrode active material and a vinylidene fluoride copolymer having a carboxy group, has low initial viscosity, and is easy to handle. It also aims to provide an electrode and a battery obtained using the electrode mixture.
  • the present invention provides an electrode mixture comprising a vinylidene fluoride copolymer having a structural unit derived from vinylidene fluoride and a structural unit derived from a vinyl compound having a carboxy group, and an electrode active material coated with carbon, wherein the amount of carbon coating on the electrode active material is 0.5% by mass or more and 3.0% by mass or less, relative to the mass of the electrode active material; the vinylidene fluoride copolymer has a weight-average molecular weight Mwa of 50,000 or more; and when the vinylidene fluoride copolymer is modified with a labeling substance consisting of 1-bromomethylpyrene to specify the weight-average molecular weight Mwc of the carboxy group-containing vinylidene fluoride copolymer that absorbs light at a wavelength of 345 nm, the Mwc is less than 0.90 relative to the Mwa.
  • the present invention provides the electrode mixture according to [1], wherein the Mwc is 0.25 or more relative to the Mwa. [3] The present invention provides the electrode mixture according to [1] or [2], wherein the average particle size of the electrode active material is 15 ⁇ m or less. [4] The present invention provides the electrode mixture according to any one of [1] to [3], wherein the amount of carbon coating on the electrode active material is 2.5 mass % or less.
  • the present invention provides an electrode comprising the solid content of the electrode mixture according to any one of [1] to [6] above.
  • the present invention provides a battery comprising the electrode according to the above [7].
  • the present invention provides an electrode mixture that contains a carbon-coated electrode active material and a vinylidene fluoride copolymer having a carboxy group, has low initial viscosity, and is easy to handle. Furthermore, electrodes and batteries obtained using the electrode mixture are also provided.
  • the electrode mix of the present invention is a slurry composition containing a vinylidene fluoride copolymer having structural units derived from vinylidene fluoride and structural units derived from a vinyl compound having a carboxy group, and a carbon-coated electrode active material (hereinafter also simply referred to as "active material").
  • the electrode mix may further contain a conductive aid, a solvent, other additives, etc.
  • the vinylidene fluoride copolymer may be dissolved in the solvent or may be dispersed in the solvent.
  • an electrode mixture (slurry) is prepared by mixing a vinylidene fluoride copolymer having carboxy groups with a carbon-coated active material (e.g., LFP or LFMP)
  • a carbon-coated active material e.g., LFP or LFMP
  • the viscosity tends to be very high, particularly the initial viscosity, and the thixotropy tends to be high.
  • "initial viscosity” refers to the slurry viscosity immediately after stirring.
  • LFP and LFMP are small-particle, carbon-coated active materials with large surface areas and numerous functional groups, such as OH groups, present on the surface. Therefore, these functional groups tend to interact with the carboxy groups of the vinylidene fluoride copolymer.
  • the electrode mixture of the present invention despite containing a vinylidene fluoride copolymer having carboxy groups and a carbon-coated electrode active material, tends to have a low initial viscosity and good thixotropy. The reasons for this are as follows:
  • the vinylidene fluoride copolymer contained in the electrode mixture of the present invention is a copolymer of at least vinylidene fluoride and a vinyl compound having a carboxy group, and is an aggregate of numerous polymers.
  • the weight-average molecular weight Mwa of the vinylidene fluoride copolymer is 50,000 or more.
  • the vinylidene fluoride copolymer includes a polymer containing structural units derived from vinylidene fluoride and structural units derived from vinyl compounds (referred to herein as a "carboxy group-containing vinylidene fluoride copolymer” or “carboxy group-containing copolymer”), and a polymer composed primarily of structural units derived from vinylidene fluoride and not containing structural units derived from vinyl compounds.
  • the weight-average molecular weight Mwc of the carboxy group-containing copolymer determined by the method described below, is less than 0.90 times the Mwa.
  • the carboxy group-containing copolymer exists in a relatively low molecular weight range compared to the molecular weight distribution of the vinylidene fluoride copolymer. If the molecular weight of the carboxyl group-containing copolymer is relatively small, it is difficult for the carboxyl group-containing copolymer to interact with the functional groups on the surface of the active material, making it difficult to form a strong network, and it is thought that the viscosity (initial viscosity) of the slurry is unlikely to increase excessively.
  • the vinylidene fluoride copolymer contained in the electrode mixture of the present invention its physical properties, and the active material and other components.
  • the vinylidene fluoride copolymer is a copolymer obtained by copolymerizing at least vinylidene fluoride and a vinyl compound having a carboxy group.
  • the amount of vinylidene fluoride-derived structural units in the vinylidene fluoride copolymer is 90.00 mol% or more, preferably 95.00 mol% or more and 99.98 mol% or less, relative to 100.00 mol% of all structural units of the vinylidene fluoride copolymer.
  • the amount of vinylidene fluoride-derived structural units is 90.0 mol% or more, physical properties specific to vinylidene fluoride are more likely to be obtained. This value can be calculated, for example, by specifying the amount of structural units derived from compounds other than vinylidene fluoride contained in the vinylidene fluoride copolymer.
  • the amount of structural units derived from a vinyl compound having a carboxy group in the vinylidene fluoride copolymer is preferably 0.01 mol% or more and 0.80 mol% or less, and preferably 0.02 mol% or more and 0.50 mol% or less, relative to 100.0 mol% of all structural units of the vinylidene fluoride copolymer.
  • the amount of structural units derived from a vinyl compound is 0.01 mol% or more, when an electrode is formed using the electrode mixture, the adhesion of the vinylidene fluoride copolymer to the current collector is likely to be further improved.
  • the amount of structural units derived from the vinyl compound is 0.80 mol% or less, the increase in the initial viscosity of the electrode mixture is more likely to be suppressed.
  • the amount of structural units derived from a vinyl compound can be determined by neutralization titration or 1H -NMR spectroscopy, etc.
  • the structure of the vinyl compound is not particularly limited, as long as it has a vinyl group polymerizable with vinylidene fluoride and a carboxy group.
  • the number of carboxy groups contained in the vinyl compound may be one or two or more.
  • an acid anhydride structure composed of two carboxy groups is also considered to be a type of carboxy group.
  • the vinylidene fluoride copolymer may contain only one type of structural unit derived from the vinyl compound, or may contain two or more types.
  • Examples of preferred vinyl compounds include compounds represented by the following general formula (1):
  • R 1 , R 2 , and R 3 each independently represent a hydrogen atom, a halogen atom, or an alkyl group having 1 to 5 carbon atoms.
  • alkyl group having 1 to 5 carbon atoms examples include linear or branched alkyl groups, specific examples of which include a methyl group, an ethyl group, a propyl group, an isopropyl group, an n-butyl group, a sec-butyl group, an isobutyl group, a t-butyl group, and a pentyl group.
  • a methyl group, an ethyl group, or a butyl group is preferred.
  • R 1 , R 2 , and R 3 each independently represent a hydrogen atom or a methyl group.
  • X is a hydroxy group or a group represented by -Y-COOH.
  • Y represents an atomic group
  • Y is preferably an atomic group containing either an oxygen atom or a nitrogen atom, more preferably an atomic group containing either an oxygen atom or a nitrogen atom, more preferably an atomic group containing either an oxygen atom or a nitrogen atom and having 1 to 10 atoms in the main chain, and preferably a divalent atomic group having a molecular weight of 500 or less and containing either an oxygen atom or a nitrogen atom and having 1 to 10 atoms in the main chain.
  • the atomic group (Y) may be linear, branched, or cyclic, or may be a combination of these. Among these, it is preferable that the atomic group (Y) be linear or branched, from the viewpoint of being less likely to cause steric hindrance during polymerization with vinylidene fluoride.
  • the number of atoms in the main chain of the atomic group (Y) may be from 1 to 10, and preferably from 2 to 8.
  • the main chain of the atomic group (Y) refers to the longest chain connecting the carbonyl group in general formula (1) and the carboxy group of -Y-COOH.
  • the atomic group (Y) contains either or both of an oxygen atom and a nitrogen atom (hereinafter, these are also collectively referred to as "heteroatoms").
  • the number of heteroatoms in the atomic group (Y) is preferably 1 to 10, more preferably 1 to 5.
  • the atomic group (Y) contains two or more heteroatoms, these may be the same type of atom or different types of atoms.
  • the heteroatoms may be contained in any structure (functional group) and may be located at any position within the atomic group (Y). Examples of structures (functional groups) containing these heteroatoms include ether bonds, ester bonds, carbonyl groups, carboxy groups, amide groups, and hydroxy groups. Among these, ether bonds, ester groups, carbonyl groups, carboxy groups, amide groups, and hydroxy groups are preferred.
  • the structure of the atomic group (Y) is not particularly limited, and can be, for example, a structure in which a hydrocarbon group such as an alkylene group or an alkyl group is bonded to a structure (functional group) containing the above heteroatom.
  • the molecular weight of the atomic group (Y) may be 500 or less, and from the viewpoint of polymerization reactivity, a molecular weight of 30 or more and 200 or less is preferred.
  • compounds represented by the above general formula (1) include (meth)acrylic acid, (meth)acryloyloxyethyl succinate, (meth)acryloyloxypropyl succinate, 2-carboxyethyl (meth)acrylate, 2-carboxymethyl (meth)acrylate, (meth)acryloyloxyethyl phthalate, and (meth)acrylamide-based compounds such as N-carboxyethyl (meth)acrylamide.
  • (meth)acrylic refers to methacrylic, acrylic, or a mixture thereof
  • (meth)acrylate refers to methacrylate, acrylate, or a mixture thereof
  • (meth)acryloyl refers to methacryloyl, acryloyl, or a mixture thereof.
  • the compounds represented by the above general formula (1) are more preferably acrylic acid, acryloyloxyethyl succinate, acryloyloxypropyl succinate, 2-carboxyethyl acrylate, and 2-carboxymethyl acrylate.
  • vinyl compound having a carboxy group is not limited to the compound represented by general formula (1).
  • vinyl compounds other than the compound represented by general formula (1) include unsaturated dibasic acids such as maleic acid, fumaric acid, and itaconic acid; unsaturated dibasic acid anhydrides such as maleic anhydride and itaconic anhydride; and unsaturated dibasic acid monoesters such as monomethyl fumarate, monoethyl fumarate, monomethyl maleate, monoethyl maleate, monomethyl citraconate, monoethyl citraconate, monomethyl phthalate, monoethyl phthalate, monomethyl itaconate, and monoethyl itaconate.
  • the vinylidene fluoride copolymer may partially contain structural units derived from compounds other than vinylidene fluoride and the above vinyl compounds (other compounds) within a range that does not impair the objects and effects of the present invention.
  • the vinylidene fluoride copolymer may contain only one type of structural unit derived from the other compounds, or may contain two or more types.
  • the total amount of structural units derived from the other compounds relative to 100.0 mol% of all structural units of the vinylidene fluoride copolymer is preferably 10.0 mol% or less, more preferably 5.0 mol% or less. These amounts are determined from 19F -NMR spectrum, 1H -NMR spectrum, neutralization titration, etc.
  • Examples of other compounds include fluorine-based vinyl compounds that have a vinyl group and a fluorine atom or a fluorine-containing alkyl group in one molecule.
  • fluorine-based vinyl compounds include vinyl fluoride; trifluoroethylene; tetrafluoroethylene; chlorotrifluoroethylene; hexafluoropropylene; and perfluoroalkyl vinyl ethers, such as perfluoromethyl vinyl ether.
  • Examples of other compounds also include compounds that have a vinyl group but do not contain fluorine. Examples include unsaturated hydrocarbon compounds such as ethylene and propylene.
  • the weight-average molecular weight Mwa of the vinylidene fluoride copolymer should be 50,000 or more, preferably 200,000 or more and 4,000,000 or less, and more preferably 250,000 or more and 3,000,000 or less.
  • the weight-average molecular weight Mwa of the vinylidene fluoride copolymer is 50,000 or more, the heat resistance and strength of the electrode (electrode mixture layer) obtained using the electrode mixture tend to be good.
  • the weight-average molecular weight Mwa of the vinylidene fluoride copolymer is a polystyrene-equivalent value measured by gel permeation chromatography (GPC).
  • the eluent used is N,N-dimethylacetamide, and the weight-average molecular weight is determined using a refractive index (RI) detector.
  • Mwa is the average value of three measurements.
  • the weight-average molecular weight Mwc of the carboxyl group-containing copolymer in the vinylidene fluoride copolymer should be less than 0.90 relative to the weight-average molecular weight Mwa of the vinylidene fluoride copolymer, i.e., Mwc/Mwa ⁇ 0.90.
  • Mwc/Mwa is preferably 0.25 or greater but less than 0.90, more preferably 0.25 or greater but less than 0.85, more preferably 0.30 or greater but less than 0.70, more preferably 0.30 or greater but less than 0.60, and even more preferably 0.30 or greater but less than 0.50. As mentioned above, if this ratio is less than 0.90, the initial viscosity of the electrode mixture is unlikely to increase excessively.
  • the specific weight average molecular weight Mwc of the carboxy group-containing copolymer is preferably 10,000 or more, more preferably 25,000 or more and 4,700,000 or less, even more preferably 50,000 or more and 3,800,000 or less, and particularly preferably 63,000 or more and 2,800,000 or less.
  • the weight average molecular weight Mwc of the carboxy group-containing copolymer is within this range, the above ratio (Mwc/Mwa) tends to fall within the desired range.
  • the weight-average molecular weight Mwc of the carboxyl group-containing copolymer is a value measured as follows.
  • a labeling substance (1-bromomethylpyrene) for labeling the carboxyl groups and potassium carbonate are mixed with a vinylidene fluoride copolymer to esterify the carboxyl groups, resulting in a pyrene-modified vinylidene fluoride copolymer.
  • GPC measurement is then performed using an ultraviolet-visible (UV-visible) detector (detection wavelength: 345 nm) and N,N-dimethylacetamide as the eluent, resulting in a polystyrene-equivalent value.
  • UV-visible ultraviolet-visible
  • the pyrene structure has characteristic absorption in the ultraviolet-visible region, strongly absorbing light at a wavelength of 345 nm.
  • the weight-average molecular weight Mwc of the carboxyl group-containing copolymer is determined by esterifying the carboxyl groups with 1-bromomethylpyrene. Mwc is the average of three measurements.
  • ⁇ i (1/C) ⁇ ln( ⁇ / ⁇ 0 )
  • is the viscosity of the solution
  • ⁇ 0 is the viscosity of the solvent N,N-dimethylformamide alone
  • C is the concentration of vinylidene fluoride copolymer in the solution, ie, 0.4 g/dl.
  • the amount of vinylidene fluoride copolymer contained in the solid content of the electrode mixture is preferably 0.2% by mass or more and 20% by mass or less, more preferably 0.2% by mass or more and 10% by mass or less, and even more preferably 0.2% by mass or more and 5% by mass or less.
  • the amount of vinylidene fluoride copolymer is within this range, a mixture layer with high strength is more likely to be obtained.
  • the vinylidene fluoride copolymer can be prepared by copolymerizing vinylidene fluoride with the vinyl compound having a carboxy group, and, if necessary, other compounds.
  • copolymerization methods include suspension polymerization, emulsion polymerization, and solution polymerization, but suspension polymerization is preferred from the viewpoint of reducing impurities.
  • suspending agents such as methyl cellulose, propoxylated methyl cellulose, hydroxyethyl cellulose, hydroxypropyl cellulose, polyvinyl alcohol, polyethylene oxide, and gelatin are added in an amount of 0.005 to 1.0 part by mass, preferably 0.01 to 0.4 part by mass, per 100 parts by mass of all monomers used in the copolymerization (vinylidene fluoride, vinyl compounds with carboxy groups, and other monomers).
  • Polymerization initiators that can be used include diisopropyl peroxydicarbonate, di-normal propyl peroxydicarbonate, di-normal heptafluoropropyl peroxydicarbonate, isobutyryl peroxide, di(chlorofluoroacyl) peroxide, di(perfluoroacyl) peroxide, and t-butyl peroxypivalate.
  • the amount used is 0.05 to 10 parts by mass, preferably 0.15 to 5 parts by mass, based on 100 parts by mass of all monomers used in the copolymerization (vinylidene fluoride, vinyl compound having a carboxy group, and other monomers as needed).
  • a chain transfer agent such as ethyl acetate, methyl acetate, diethyl carbonate, acetone, ethanol, n-propanol, acetaldehyde, propylaldehyde, ethyl propionate, or carbon tetrachloride.
  • a chain transfer agent such as ethyl acetate, methyl acetate, diethyl carbonate, acetone, ethanol, n-propanol, acetaldehyde, propylaldehyde, ethyl propionate, or carbon tetrachloride.
  • the amount used is typically 0.01 to 5 parts by mass, and preferably 0.01 to 3 parts by mass, per 100 parts by mass of all monomers used in the copolymerization (vinylidene fluoride, vinyl compounds having carboxy groups, and any other monomers).
  • the polymerization temperature T is appropriately selected depending on the 10-hour half-life temperature T10 of the polymerization initiator, and is usually selected within the range of T10 -25°C ⁇ T ⁇ T10 +25°C.
  • the T10 of t-butyl peroxypivalate and diisopropyl peroxydicarbonate are 54.6°C and 40.5°C, respectively (see NOF Corporation product catalog). Therefore, in polymerizations using t-butyl peroxypivalate and diisopropyl peroxydicarbonate as polymerization initiators, the polymerization temperature T is appropriately selected within the ranges of 29.6°C ⁇ T ⁇ 79.6°C and 15.5°C ⁇ T ⁇ 65.5°C, respectively.
  • the polymerization time is not particularly limited, but is preferably 100 hours or less in consideration of productivity, etc.
  • the polymerization is usually carried out under increased pressure, preferably 2.0 to 10.0 MPa-G.
  • the active material contained in the electrode mixture of the present invention is a carbon-coated compound, and the amount of carbon coating is 0.5% by mass or more and 3.0% by mass or less relative to the mass of the active material.
  • the amount of carbon coating is determined by heating and dissolving each positive electrode material in aqua regia, suction filtering through a membrane filter, and calculating the acid-insoluble content (carbon amount) from the amount remaining on the filter.
  • the amount of carbon coating is preferably 0.5% by mass or more and 2.7% by mass or less, and more preferably 0.5% by mass or more and 2.5% by mass or less.
  • the type of active material is not particularly limited as long as the above-mentioned carbon coating amount is satisfied.
  • olivine- type lithium compounds represented by LiMaPO4 (where Ma is one or more elements selected from Co, Ni, Mn, Fe, Mg, Nb, Ti, Al, and Zr), such as LiFePO4 ( LFP ) and LiFeMnPO4 (LFMP), which are positive electrode active materials, often have their surfaces carbon-coated to reduce particle resistance, making it easy to satisfy the above-mentioned coverage rate.
  • LiMaPO4 where Ma is one or more elements selected from Co, Ni, Mn, Fe, Mg, Nb, Ti, Al, and Zr
  • LiFePO4 LFP
  • LiFeMnPO4 LiFeMnPO4
  • the initial viscosity tends to increase.
  • the initial viscosity of the electrode mixture is less likely to increase.
  • the above-mentioned LFP and LFMP have a relatively small average particle diameter.
  • the average particle diameter of the active material in the electrode mixture is small, the initial viscosity of the electrode mixture is usually likely to increase.
  • the vinylidene fluoride copolymer it is difficult for the vinylidene fluoride copolymer to form a strong network structure starting from the active material. Therefore, even if the average particle diameter of LFP or LFMP is small, the initial viscosity of the electrode mixture is unlikely to increase.
  • the average particle diameter of the active material is the particle diameter at which the particle size cumulative ratio is 50% in a volume-based particle size cumulative diagram (based on JIS K 1474).
  • the average particle diameter Dv50 of the active material can be 15 ⁇ m or less, for example, 0.1 ⁇ m or more and 15 ⁇ m or less. However, the average particle diameter of the active material is not limited to this range.
  • the amount of active material contained in the electrode mixture is selected appropriately depending on the application of the electrode mixture, but is preferably 50% by mass or more and 99.9% by mass or less of the total solid content of the electrode mixture. When the amount of active material is within this range, for example, sufficient charge/discharge capacity can be obtained, and battery performance is likely to be good.
  • the electrode mixture may further contain a conductive additive.
  • the conductive additive contained in the electrode mixture is not particularly limited as long as it is a compound that can further increase the conductivity between the active materials or between the active material and the current collector.
  • Examples of the conductive additive include acetylene black, ketjen black, carbon black, graphite powder, carbon nanofiber, carbon nanotube, and carbon fiber.
  • the amount of conductive additive contained in the electrode mixture is selected appropriately depending on the type of conductive additive. From the perspective of improving both the conductivity and the dispersibility of the conductive additive, the amount is preferably 0.1% to 15% by mass, more preferably 0.1% to 7% by mass, and even more preferably 0.1% to 5% by mass, relative to the total amount of solids in the electrode mixture.
  • the electrode mixture may contain a solvent.
  • the solvent may be a non-aqueous solvent or water.
  • the non-aqueous solvent may also be a polar solvent (polar solvent).
  • the polar solvent include amide compounds such as N,N-dimethylformamide, N,N-dimethylacetamide, and N-methylpyrrolidone; alcohol compounds such as methanol, ethanol, isopropyl alcohol, 2-ethyl-1-hexanol, 1-nonanol, lauryl alcohol, and tripropylene glycol; amine compounds such as o-toluidine, m-toluidine, and p-toluidine; imide compounds such as 1-ethyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide; lactone compounds such as ⁇ -butyrolactone and ⁇ -butyrolactone; sulfoxide/sulfone compounds such as dimethyl sulfoxide and sulf
  • the total amount of solvent in the electrode mixture is not particularly limited, but is typically preferably 10 to 150 parts by weight per 100 parts by weight of the active material.
  • the electrode mixture may further contain a dispersant, an adhesive aid, a thickener, etc., and known compounds can be used for these.
  • the dispersant include polyvinylpyrrolidone, methylcellulose, methoxylated methylcellulose, propoxylated methylcellulose, hydroxyethyl cellulose, hydroxypropyl cellulose, polyvinyl alcohol, polyethylene oxide, polypropylene oxide, gelatin, etc.
  • the adhesive aid include poly(meth)acrylic acid, metal salts of poly(meth)acrylic acid such as sodium poly(meth)acrylate, carboxymethyl cellulose, etc. The amount of these is not particularly limited as long as it does not impair the object and effect of the present invention, but is preferably 15 mass% or less based on the total solid content of the electrode mixture.
  • the viscosity of the electrode mixture is not particularly limited as long as it can prevent dripping, uneven coating, and delayed drying after coating when applying the electrode mixture to form a mixture layer, and provides good workability and applicability when preparing the mixture layer.
  • the value of the electrode mixture measured at 25 ° C. using an E-type viscometer is measured after a 60-second incubation period at 25 ° C., rotating the rotor at a shear rate of 1 s ⁇ 1 , and measuring 120 seconds after the start of rotor rotation.
  • the value is preferably 2000 mPa s or more and 60,000 mPa s or less, more preferably 5,000 mPa s or more and 30,000 mPa s or less. When the initial viscosity is within this range, handling when forming the mixture layer tends to be even better.
  • Weight average molecular weight Mwa of vinylidene fluoride copolymer The weight-average molecular weight Mw1 of the vinylidene fluoride copolymer prepared in each Example and Comparative Example was measured using a differential refractometer (RI). Specifically, GPC (gel permeation chromatography) was performed under the following conditions, and Mwa was determined using a differential refractive index detector. This was performed three times, and the average value was taken as Mwa.
  • RI differential refractometer
  • the weight-average molecular weight of the carboxyl group-containing copolymer (a polymer that absorbs light at a wavelength of 345 nm) contained in the vinylidene fluoride copolymer labeled with 1-bromomethylpyrene was determined using a UV-vis detector. The measurement was carried out under the same conditions as for Mwa above, except for the detector. The detection wavelength was 345 nm, and the weight-average molecular weight Mwc of the carboxyl group-containing copolymer was determined. This was carried out three times, and the average value was taken as Mwc.
  • the rotor was rotated at a shear rate of 40 s ⁇ 1 , and the viscosity 30 seconds after the rotor started to rotate was determined as the slurry viscosity. Also, the viscosity ratio of the specified slurry viscosity at a shear rate of 1 s ⁇ 1 to the slurry viscosity at a shear rate of 40 s ⁇ 1 (slurry viscosity at a shear rate of 1 s ⁇ 1 /slurry viscosity at a shear rate of 40 s ⁇ 1 ) was specified.
  • VDF/APS-1 Vinylidene fluoride copolymers
  • VDF/APS-2 Prepared in Synthesis Example 2 below
  • VDF/AA-1 Prepared in Synthesis Example 3 below
  • VDF/AA-2 Prepared in Synthesis Example 4 below
  • VDF/APS-1 vinylidene fluoride copolymer
  • VDF vinylidene fluoride copolymer
  • APS acryloyloxypropyl succinic acid
  • VDF/APS-2 vinylidene fluoride copolymer
  • VDF vinylidene fluoride copolymer
  • APS acryloyloxypropyl succinic acid
  • Example 1 LFP:A was used as the electrode active material, VDF/APS-1 was used as the vinylidene fluoride copolymer (binder), and a carbon nanotube (CNT) NMP dispersion was used as the conductive additive. These were then mixed using a planetary centrifugal mixer, Thinky Mixer ARE310, to prepare an electrode mixture.
  • the mass ratio of the electrode active material, conductive additive, and binder in the resulting electrode mixture was 100:2:2.5, and the solids concentration was 55.0 mass%.
  • the slurry viscosity at this time is shown in Table 2.
  • Example 2 Comparative Examples 1 to 5, and Reference Examples 1 and 2
  • electrode mixtures were prepared in the same manner as in Example 1 above, except that the type of electrode active material, the type of vinylidene fluoride copolymer, and the solid content concentration in Example 4 and Comparative Example 4 were changed to 52%.
  • an electrode mixture that contains a carbon-coated electrode active material and a vinylidene fluoride copolymer having a carboxy group, has a low initial viscosity, and is easy to handle.
  • the electrode mixture is very useful in the field of manufacturing various batteries.

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Abstract

The present invention addresses the problem of providing an electrode mixture containing an electrode active material coated with carbon, and a vinylidene fluoride copolymer having a carboxy group, the electrode mixture having low initial viscosity and excellent handleability. This electrode mixture for addressing the aforementioned problem contains a vinylidene fluoride copolymer having a constituent unit derived from vinylidene fluoride and a constituent unit derived from a vinyl compound having a carboxy group, and an electrode active material coated with carbon. The carbon coating amount of the electrode active material is 0.5-3.0 mass% with respect to the mass of the electrode active material, and the weight-average molecular weight Mwa of the vinylidene fluoride copolymer is 50,000 or greater. When the vinylidene fluoride copolymer is modified with a labeling substance composed of 2-bromomethylpyrene and the weight-average molecular weight Mwc of a carboxy-group-containing vinylidene fluoride copolymer that absorbs light having a wavelength of 345 nm is identified, Mwc is less than 0.90 with respect to Mwa.

Description

電極合剤、電極、および電池Electrode mixture, electrode, and battery

 本発明は、電極合剤、電極、および電池に関する。 The present invention relates to an electrode mixture, an electrode, and a battery.

 非水電解質二次電池の電極の合剤層の形成には、通常、バインダー(結着剤)および活物質を含む電極合剤が用いられる。上記バインダー(結着剤)としては、フッ化ビニリデン重合体が主に使用されている。バインダーには、活物質を集電体に接着させるという役割から、高接着性が求められている。例えば特許文献1には、フッ素系樹脂にカルボキシ基等の官能基を導入し、集電体等への接着性を改良したり、溶媒への溶解性を改良することが記載されている。特許文献2にはフッ化ビニリデンと、特定の構造の化合物との共重合体(フッ化ビニリデン共重合体)を含むバインダー組成物が記載されており、当該フッ化ビニリデン共重合体が、集電体に対して高い接着性を示すことが記載されている。 An electrode mixture containing a binder and active material is typically used to form the mixture layer of an electrode in a non-aqueous electrolyte secondary battery. Vinylidene fluoride polymer is typically used as the binder. High adhesiveness is required for the binder, as it serves the purpose of adhering the active material to the current collector. For example, Patent Document 1 describes introducing functional groups such as carboxyl groups into a fluorine-based resin to improve adhesion to the current collector and solubility in solvents. Patent Document 2 describes a binder composition containing a copolymer of vinylidene fluoride and a compound with a specific structure (vinylidene fluoride copolymer), and describes that the vinylidene fluoride copolymer exhibits high adhesion to the current collector.

 一方、電池の低コスト化を目的として、リン酸鉄リチウム(LFP)を正極活物質として用いることが検討されている。また、次世代材料として、リン酸鉄マンガンリチウム(LFMP)の正極活物質としての使用も検討されている。 Meanwhile, with the aim of reducing battery costs, the use of lithium iron phosphate (LFP) as a positive electrode active material is being considered. Furthermore, the use of lithium iron manganese phosphate (LFMP) as a next-generation material as a positive electrode active material is also being considered.

特開平6-172452号公報Japanese Patent Application Publication No. 6-172452 特許第5797206号公報Patent No. 5797206

 集電体等に対する接着性を高めるため、上記リン酸鉄リチウム(LFP)や、リン酸鉄マンガンリチウム(LFMP)を含む電極合剤(スラリー)にも、上述の特許文献1や特許文献2に記載のフッ化ビニリデン共重合体を電極用バインダーとして用いることが考えられる。しかしながら、LFPやLFMPと、集電体に対する接着強度が高いフッ化ビニリデン共重合体と、を混合すると、電極合剤の初期粘度が高くなり、チキソトロピー性が大きくなりやすかった。そして、このような電極合剤では、電極の作製が非常に難しかった。本発明者らが鋭意検討したところ、LFPやLFMPを含む電極合剤において、初期粘度が高まったり、チキソトロピー性が高くなりやすい理由としては、LFPやLFMPの表面に存在する炭素被覆、およびカルボキシ基を有するフッ化ビニリデン共重合体が相互作用すると考えられる。 In order to improve adhesion to current collectors, etc., it is conceivable to use the vinylidene fluoride copolymer described in Patent Documents 1 and 2 as an electrode binder in electrode mixtures (slurries) containing the above-mentioned lithium iron phosphate (LFP) or lithium iron manganese phosphate (LFMP). However, when LFP or LFMP is mixed with a vinylidene fluoride copolymer, which has high adhesive strength to current collectors, the initial viscosity of the electrode mixture increases and thixotropy tends to become stronger. Furthermore, it is extremely difficult to fabricate electrodes using such electrode mixtures. After extensive research, the inventors have determined that the reason for the increased initial viscosity and increased thixotropy in electrode mixtures containing LFP or LFMP is believed to be due to an interaction between the carbon coating present on the surface of the LFP or LFMP and the vinylidene fluoride copolymer containing carboxyl groups.

 本発明は、上記課題を鑑みてなされたものである。本発明は、炭素で被覆された電極活物質、およびカルボキシ基を有するフッ化ビニリデン共重合体を含み、初期粘度が低く、かつ取扱性が良好な電極合剤の提供を目的とする。また、当該電極合剤を用いて得られる電極、および電池の提供も目的とする。 The present invention was made in consideration of the above-mentioned problems. It aims to provide an electrode mixture that contains a carbon-coated electrode active material and a vinylidene fluoride copolymer having a carboxy group, has low initial viscosity, and is easy to handle. It also aims to provide an electrode and a battery obtained using the electrode mixture.

 [1]本発明は、フッ化ビニリデン由来の構成単位、およびカルボキシ基を有するビニル化合物由来の構成単位、を有するフッ化ビニリデン共重合体と、炭素で被覆された電極活物質と、を含む電極合剤であり、前記電極活物質の炭素被覆量が、前記電極活物質の質量に対して0.5質量%以上3.0質量%以下であり、前記フッ化ビニリデン共重合体の重量平均分子量Mwaが50000以上であり、前記フッ化ビニリデン共重合体を、1-ブロモメチルピレンからなる標識物質で修飾し、波長345nmの光を吸収するカルボキシ基含有フッ化ビニリデン共重合体の重量平均分子量Mwcを特定したとき、前記Mwcが、前記Mwaに対して、0.90未満である、電極合剤を提供する。
 [2]本発明は、前記Mwcが、前記Mwaに対して、0.25以上である、[1]に記載の電極用合剤を提供する。
 [3]本発明は、前記電極活物質の平均粒子径が15μm以下である、[1]または[2]に記載の電極合剤を提供する。
 [4]本発明は、前記電極活物質は、前記炭素被覆量が2.5質量%以下である、[1]~[3]のいずれかに記載の電極合剤を提供する。
 [5]本発明は、前記ビニル化合物が、下記一般式(1)で表される化合物である、[1]~[4]に記載の電極合剤を提供する。
(一般式(1)において、R、R、Rはそれぞれ独立に、水素原子、ハロゲン原子、または炭素数1以上5以下のアルキル基を表し、Xは、ヒドロキシ基、または-Y-COOHを表す(Yは原子団を表す))
 [6]本発明は、前記ビニル化合物が、下記一般式(1)で表される化合物である、[1]~[4]のいずれかに記載の電極合剤を提供する。
(一般式(1)において、R、R、Rはそれぞれ独立に、水素原子、ハロゲン原子、または炭素数1以上5以下のアルキル基を表し、Xは、ヒドロキシ基、または-Y-COOHを表す(Yは酸素原子または窒素原子のいずれか一方を含み、かつ主鎖の原子数が1以上10以下である、分子量500以下の2価の原子団を表す))
[1] The present invention provides an electrode mixture comprising a vinylidene fluoride copolymer having a structural unit derived from vinylidene fluoride and a structural unit derived from a vinyl compound having a carboxy group, and an electrode active material coated with carbon, wherein the amount of carbon coating on the electrode active material is 0.5% by mass or more and 3.0% by mass or less, relative to the mass of the electrode active material; the vinylidene fluoride copolymer has a weight-average molecular weight Mwa of 50,000 or more; and when the vinylidene fluoride copolymer is modified with a labeling substance consisting of 1-bromomethylpyrene to specify the weight-average molecular weight Mwc of the carboxy group-containing vinylidene fluoride copolymer that absorbs light at a wavelength of 345 nm, the Mwc is less than 0.90 relative to the Mwa.
[2] The present invention provides the electrode mixture according to [1], wherein the Mwc is 0.25 or more relative to the Mwa.
[3] The present invention provides the electrode mixture according to [1] or [2], wherein the average particle size of the electrode active material is 15 μm or less.
[4] The present invention provides the electrode mixture according to any one of [1] to [3], wherein the amount of carbon coating on the electrode active material is 2.5 mass % or less.
[5] The present invention provides the electrode mixture according to any one of [1] to [4], wherein the vinyl compound is a compound represented by the following general formula (1):
(In general formula (1), R 1 , R 2 , and R 3 each independently represent a hydrogen atom, a halogen atom, or an alkyl group having 1 to 5 carbon atoms, and X represents a hydroxy group or —Y—COOH (Y represents an atomic group).)
[6] The present invention provides the electrode mixture according to any one of [1] to [4], wherein the vinyl compound is a compound represented by the following general formula (1):
(In general formula (1), R 1 , R 2 , and R 3 each independently represent a hydrogen atom, a halogen atom, or an alkyl group having 1 to 5 carbon atoms, and X represents a hydroxy group or —Y—COOH (Y represents a divalent atomic group containing either an oxygen atom or a nitrogen atom, having 1 to 10 atoms in the main chain, and having a molecular weight of 500 or less).)

 [7]本発明は、上記[1]~[6]のいずれかに記載の電極合剤の固形分を含む、電極を提供する。
 [8]本発明は、上記[7]に記載の電極を含む、電池を提供する。
[7] The present invention provides an electrode comprising the solid content of the electrode mixture according to any one of [1] to [6] above.
[8] The present invention provides a battery comprising the electrode according to the above [7].

 本発明によれば、炭素で被覆された電極活物質、およびカルボキシ基を有するフッ化ビニリデン共重合体を含み、初期粘度が低く、かつ取扱性が良好な電極合剤が提供される。さらに、当該電極合剤を用いて得られる電極、および電池も提供される。 The present invention provides an electrode mixture that contains a carbon-coated electrode active material and a vinylidene fluoride copolymer having a carboxy group, has low initial viscosity, and is easy to handle. Furthermore, electrodes and batteries obtained using the electrode mixture are also provided.

 1.電極合剤
 本発明の電極合剤は、フッ化ビニリデン由来の構成単位、およびカルボキシ基を有するビニル化合物由来の構成単位を有するフッ化ビニリデン共重合体と、炭素で被覆された電極活物質(以下、単に「活物質」とも称する)と、を含むスラリー状の組成物である。当該電極合剤は、導電助剤や、溶媒、その他の添加剤等をさらに含んでいてもよい。電極合剤が溶媒を含む場合、フッ化ビニリデン共重合体は、溶媒に溶解していてもよいし、溶媒に分散していてもよい。
1. Electrode Mix The electrode mix of the present invention is a slurry composition containing a vinylidene fluoride copolymer having structural units derived from vinylidene fluoride and structural units derived from a vinyl compound having a carboxy group, and a carbon-coated electrode active material (hereinafter also simply referred to as "active material"). The electrode mix may further contain a conductive aid, a solvent, other additives, etc. When the electrode mix contains a solvent, the vinylidene fluoride copolymer may be dissolved in the solvent or may be dispersed in the solvent.

 上述のように、カルボキシ基を有するフッ化ビニリデン共重合体と、炭素で被覆された活物質(例えばLFP、LFMP)とを混合して電極合剤(スラリー)を調製すると、粘度が非常に高くなりやすく、特に初期粘度が高くなりやすく、チキソトロピー性も高くなりやすかった。本明細書において、初期粘度とは、スラリーを攪拌した直後におけるスラリー粘度をいう。一般的に、LFPやLFMPなどは、小粒径且つ、炭素によって被覆された活物質であり、表面積が大きく、表面には、OH基等の官能基が多く存在する。そのため、フッ化ビニリデン共重合体のカルボキシ基とこれらの官能基が相互しやすく、一般的なフッ化ビニリデン共重合体を用いた場合には、電極合剤内で、活物質を起点とした強固なネットワークが形成されて増粘が生じる。これに対し、本発明の電極合剤は、上記のように、カルボキシ基を有するフッ化ビニリデン共重合体、および炭素で被覆された電極活物質を含むにも拘わらず、初期粘度が低く、かつチキソトロピー性も良好になりやすい。その理由としては、以下の点が挙げられる。 As described above, when an electrode mixture (slurry) is prepared by mixing a vinylidene fluoride copolymer having carboxy groups with a carbon-coated active material (e.g., LFP or LFMP), the viscosity tends to be very high, particularly the initial viscosity, and the thixotropy tends to be high. In this specification, "initial viscosity" refers to the slurry viscosity immediately after stirring. Generally, LFP and LFMP are small-particle, carbon-coated active materials with large surface areas and numerous functional groups, such as OH groups, present on the surface. Therefore, these functional groups tend to interact with the carboxy groups of the vinylidene fluoride copolymer. When a typical vinylidene fluoride copolymer is used, a strong network originating from the active material forms within the electrode mixture, resulting in increased viscosity. In contrast, the electrode mixture of the present invention, despite containing a vinylidene fluoride copolymer having carboxy groups and a carbon-coated electrode active material, tends to have a low initial viscosity and good thixotropy. The reasons for this are as follows:

 本発明の電極合剤が含むフッ化ビニリデン共重合体は、少なくともフッ化ビニリデンと、カルボキシ基を有するビニル化合物とを共重合したものであり、多数のポリマーの集合体である。当該フッ化ビニリデン共重合体の重量平均分子量Mwaは50000以上である。また、当該フッ化ビニリデン共重合体は、フッ化ビニリデン由来の構成単位およびビニル化合物由来の構成単位を含むポリマー(本明細書では、「カルボキシ基含有フッ化ビニリデン共重合体」もしくは「カルボキシ基含有共重合体」と称する)と、主にフッ化ビニリデン由来の構成単位で構成され、ビニル化合物由来の構成単位を含まないポリマーと、を含む。そして、後述の方法で特定される、カルボキシ基含有共重合体の重量平均分子量Mwcが、上記Mwaに対して0.90未満である。つまり、フッ化ビニリデン共重合体の分子量分布に対し、カルボキシ基含有共重合体は相対的に低分子量域に存在している。カルボキシ基含有共重合体の分子量が相対的に小さいと、カルボキシ基含有共重合体と活物質表面の官能基とが相互作用し難くなり、強固なネットワークが形成され難いため、スラリーの粘度(初期粘度)が過度に高まり難いと考えられる。以下、本発明の電極合剤が含む、フッ化ビニリデン共重合体や、その物性、さらに活物質やその他の成分等について、詳しく説明する。 The vinylidene fluoride copolymer contained in the electrode mixture of the present invention is a copolymer of at least vinylidene fluoride and a vinyl compound having a carboxy group, and is an aggregate of numerous polymers. The weight-average molecular weight Mwa of the vinylidene fluoride copolymer is 50,000 or more. The vinylidene fluoride copolymer includes a polymer containing structural units derived from vinylidene fluoride and structural units derived from vinyl compounds (referred to herein as a "carboxy group-containing vinylidene fluoride copolymer" or "carboxy group-containing copolymer"), and a polymer composed primarily of structural units derived from vinylidene fluoride and not containing structural units derived from vinyl compounds. The weight-average molecular weight Mwc of the carboxy group-containing copolymer, determined by the method described below, is less than 0.90 times the Mwa. In other words, the carboxy group-containing copolymer exists in a relatively low molecular weight range compared to the molecular weight distribution of the vinylidene fluoride copolymer. If the molecular weight of the carboxyl group-containing copolymer is relatively small, it is difficult for the carboxyl group-containing copolymer to interact with the functional groups on the surface of the active material, making it difficult to form a strong network, and it is thought that the viscosity (initial viscosity) of the slurry is unlikely to increase excessively. Below, we will explain in detail the vinylidene fluoride copolymer contained in the electrode mixture of the present invention, its physical properties, and the active material and other components.

 (フッ化ビニリデン共重合体)
 フッ化ビニリデン共重合体は、上述のように、フッ化ビニリデンとカルボキシ基を有するビニル化合物とを少なくとも共重合した共重合体である。フッ化ビニリデン共重合体中のフッ化ビニリデン由来の構成単位の量は、フッ化ビニリデン共重合体の全構成単位100.00モル%に対して90.00モル%以上であり、95.00モル%以上99.98モル%以下が好ましい。フッ化ビニリデン由来の構成単位の量が、90.0モル%以上であると、フッ化ビニリデン特有の物性が得られやすくなる。当該数値は、例えばフッ化ビニリデン共重合体が含む、フッ化ビニリデン以外の化合物由来の構成単位の量を特定することで算出可能である。
(Vinylidene fluoride copolymer)
As described above, the vinylidene fluoride copolymer is a copolymer obtained by copolymerizing at least vinylidene fluoride and a vinyl compound having a carboxy group. The amount of vinylidene fluoride-derived structural units in the vinylidene fluoride copolymer is 90.00 mol% or more, preferably 95.00 mol% or more and 99.98 mol% or less, relative to 100.00 mol% of all structural units of the vinylidene fluoride copolymer. When the amount of vinylidene fluoride-derived structural units is 90.0 mol% or more, physical properties specific to vinylidene fluoride are more likely to be obtained. This value can be calculated, for example, by specifying the amount of structural units derived from compounds other than vinylidene fluoride contained in the vinylidene fluoride copolymer.

 一方、上記フッ化ビニリデン共重合体中のカルボキシ基を有するビニル化合物由来の構成単位の量は、フッ化ビニリデン共重合体の全構成単位100.0モル%に対して0.01モル%以上0.80モル%以下が好ましく、0.02モル%以上0.50モル%以下が好ましい。ビニル化合物由来の構成単位の量が、0.01モル%以上であると、電極合剤を用いて電極を形成した際に、フッ化ビニリデン共重合体の集電体に対する接着性がさらに高まりやすい。一方、上記ビニル化合物由来の構成単位の量が0.80モル%以下であると、電極合剤の初期粘度の上昇をさらに抑制しやすくなる。ビニル化合物由来の構成単位の量は、中和滴定もしくはH-NMRスペクトル等から求めることができる。 On the other hand, the amount of structural units derived from a vinyl compound having a carboxy group in the vinylidene fluoride copolymer is preferably 0.01 mol% or more and 0.80 mol% or less, and preferably 0.02 mol% or more and 0.50 mol% or less, relative to 100.0 mol% of all structural units of the vinylidene fluoride copolymer. When the amount of structural units derived from a vinyl compound is 0.01 mol% or more, when an electrode is formed using the electrode mixture, the adhesion of the vinylidene fluoride copolymer to the current collector is likely to be further improved. On the other hand, when the amount of structural units derived from the vinyl compound is 0.80 mol% or less, the increase in the initial viscosity of the electrode mixture is more likely to be suppressed. The amount of structural units derived from a vinyl compound can be determined by neutralization titration or 1H -NMR spectroscopy, etc.

 ここで、上記ビニル化合物の構造は特に制限されず、フッ化ビニリデンと重合可能なビニル基を有し、かつカルボキシ基を有する化合物であればよい。なお、ビニル化合物が含むカルボキシ基の数は1つであってもよく、2つ以上であってもよい。なお、本明細書では、2つのカルボキシ基から構成される酸無水物構造も、カルボキシ基の一種として取り扱う。フッ化ビニリデン共重合体は、当該ビニル化合物由来の構成単位を一種のみ含んでいてもよく、二種以上含んでいてもよい。好ましいビニル化合物の例には、下記一般式(1)で表される化合物が含まれる。
 一般式(1)において、R、R、Rはそれぞれ独立に、水素原子、ハロゲン原子、または炭素数1以上5以下のアルキル基を表す。炭素数1以上5以下のアルキル基の例には、直鎖状または分岐鎖状のアルキル基が含まれ、その具体例にはメチル基、エチル基、プロピル基、イソプロピル基、n-ブチル基、sec-ブチル基、イソブチル基、t-ブチル基、ペンチル基等が含まれる。これらの中でも、入手容易性等の観点で、メチル基、エチル基、またはブチル基が好ましい。また特に、フッ化ビニリデンとの重合時に立体障害が生じ難いという観点で、R、R、およびRは、それぞれ独立に、水素原子、またはメチル基であることがより好ましい。
Here, the structure of the vinyl compound is not particularly limited, as long as it has a vinyl group polymerizable with vinylidene fluoride and a carboxy group. The number of carboxy groups contained in the vinyl compound may be one or two or more. In this specification, an acid anhydride structure composed of two carboxy groups is also considered to be a type of carboxy group. The vinylidene fluoride copolymer may contain only one type of structural unit derived from the vinyl compound, or may contain two or more types. Examples of preferred vinyl compounds include compounds represented by the following general formula (1):
In general formula (1), R 1 , R 2 , and R 3 each independently represent a hydrogen atom, a halogen atom, or an alkyl group having 1 to 5 carbon atoms. Examples of the alkyl group having 1 to 5 carbon atoms include linear or branched alkyl groups, specific examples of which include a methyl group, an ethyl group, a propyl group, an isopropyl group, an n-butyl group, a sec-butyl group, an isobutyl group, a t-butyl group, and a pentyl group. Among these, from the viewpoint of ease of availability, etc., a methyl group, an ethyl group, or a butyl group is preferred. Furthermore, from the viewpoint of reducing the likelihood of steric hindrance during polymerization with vinylidene fluoride, it is more preferred that R 1 , R 2 , and R 3 each independently represent a hydrogen atom or a methyl group.

 また、上記一般式(1)において、Xは、ヒドロキシ基、または-Y-COOHで表される基である。ここで、Yは原子団を表し、Yは酸素原子または窒素原子のいずれか一方を含む原子団であることが好ましく、Yは酸素原子または窒素原子のいずれか一方を含む原子団であることがより好ましく、Yは酸素原子または窒素原子のいずれか一方を含みかつ主鎖の原子数が1以上10以下である原子団であることがより好ましく、Yは酸素原子または窒素原子のいずれか一方を含み、かつ主鎖の原子数が1以上10以下である、分子量500以下の2価の原子団であることが好ましい。 Furthermore, in the above general formula (1), X is a hydroxy group or a group represented by -Y-COOH. Here, Y represents an atomic group, and Y is preferably an atomic group containing either an oxygen atom or a nitrogen atom, more preferably an atomic group containing either an oxygen atom or a nitrogen atom, more preferably an atomic group containing either an oxygen atom or a nitrogen atom and having 1 to 10 atoms in the main chain, and preferably a divalent atomic group having a molecular weight of 500 or less and containing either an oxygen atom or a nitrogen atom and having 1 to 10 atoms in the main chain.

 当該原子団(Y)は直鎖状であってもよく、分岐鎖状であってもよく、環状構造であってもよく、これらの組み合わせであってもよい。これらの中でも、フッ化ビニリデンとの重合時に立体障害が生じ難いという観点で、当該原子団(Y)は直鎖状または分岐鎖状であることが好ましい。 The atomic group (Y) may be linear, branched, or cyclic, or may be a combination of these. Among these, it is preferable that the atomic group (Y) be linear or branched, from the viewpoint of being less likely to cause steric hindrance during polymerization with vinylidene fluoride.

 原子団(Y)の主鎖の原子数は、1以上10以下であればよく、2以上8以下が好ましい。本明細書において、原子団(Y)の主鎖とは、一般式(1)のカルボニル基と、-Y-COOHのカルボキシ基とを繋ぐ鎖のうち、最も長い鎖をいう。 The number of atoms in the main chain of the atomic group (Y) may be from 1 to 10, and preferably from 2 to 8. In this specification, the main chain of the atomic group (Y) refers to the longest chain connecting the carbonyl group in general formula (1) and the carboxy group of -Y-COOH.

 ここで、上記原子団(Y)は、酸素原子および窒素原子(以下、これらをまとめて「ヘテロ原子」とも称する)のうち、いずれか一方もしくは両方を含む。原子団(Y)中のヘテロ原子の数は、1以上10以下が好ましく、1以上5以下がより好ましい。原子団(Y)がヘテロ原子を2つ以上含む場合、これらは同種の原子であってもよく、異なる種類の原子であってもよい。ヘテロ原子は、どのような構造(官能基)に含まれていてもよく、原子団(Y)内のどの位置に存在していてもよい。これらのヘテロ原子を含む構造(官能基)の例には、エーテル結合、エステル結合、カルボニル基、カルボキシ基、アミド基、ヒドロキシ基等が含まれる。これらの中でもエーテル結合、エステル基、カルボニル基、カルボキシ基、アミド基、およびヒドロキシ基が好ましい。 Here, the atomic group (Y) contains either or both of an oxygen atom and a nitrogen atom (hereinafter, these are also collectively referred to as "heteroatoms"). The number of heteroatoms in the atomic group (Y) is preferably 1 to 10, more preferably 1 to 5. When the atomic group (Y) contains two or more heteroatoms, these may be the same type of atom or different types of atoms. The heteroatoms may be contained in any structure (functional group) and may be located at any position within the atomic group (Y). Examples of structures (functional groups) containing these heteroatoms include ether bonds, ester bonds, carbonyl groups, carboxy groups, amide groups, and hydroxy groups. Among these, ether bonds, ester groups, carbonyl groups, carboxy groups, amide groups, and hydroxy groups are preferred.

 原子団(Y)の構造は特に制限されず、例えばアルキレン基やアルキル基等の炭化水素基と、上記ヘテロ原子を含む構造(官能基)とが結合した構造とすることができる。なお、原子団(Y)の分子量は500以下であればよく、重合反応性の観点から30以上200以下が好ましい。 The structure of the atomic group (Y) is not particularly limited, and can be, for example, a structure in which a hydrocarbon group such as an alkylene group or an alkyl group is bonded to a structure (functional group) containing the above heteroatom. The molecular weight of the atomic group (Y) may be 500 or less, and from the viewpoint of polymerization reactivity, a molecular weight of 30 or more and 200 or less is preferred.

 上記一般式(1)で表される化合物の具体例には、(メタ)アクリル酸、(メタ)アクリロイロキシエチルコハク酸、(メタ)アクリロイロキシプロピルコハク酸、2-カルボキシエチル(メタ)アクリレート、2-カルボキシメチル(メタ)アクリレート、(メタ)アクリロイロキシエチルフタル酸、N-カルボキシエチル(メタ)アクリルアミド等の(メタ)アクリルアミド系化合物等が含まれる。なお、本明細書において、(メタ)アクリルとは、メタクリル、アクリル、またはこれらの混合物を表し、(メタ)アクリレートとは、メタクリレート、アクリレート、またはこれらの混合物を表し、(メタ)アクリロイルとは、メタクリロイル、アクリロイル、またはこれらの混合物を表す。 Specific examples of compounds represented by the above general formula (1) include (meth)acrylic acid, (meth)acryloyloxyethyl succinate, (meth)acryloyloxypropyl succinate, 2-carboxyethyl (meth)acrylate, 2-carboxymethyl (meth)acrylate, (meth)acryloyloxyethyl phthalate, and (meth)acrylamide-based compounds such as N-carboxyethyl (meth)acrylamide. In this specification, (meth)acrylic refers to methacrylic, acrylic, or a mixture thereof; (meth)acrylate refers to methacrylate, acrylate, or a mixture thereof; and (meth)acryloyl refers to methacryloyl, acryloyl, or a mixture thereof.

 上記一般式(1)で表される化合物は、入手容易性や、フッ化ビニリデンとの反応性等の観点で、アクリル酸、アクリロイロキシエチルコハク酸、アクリロイロキシプロピルコハク酸、、2-カルボキシエチルアクリレート、2-カルボキシメチルアクリレートがより好ましい。 In terms of availability and reactivity with vinylidene fluoride, the compounds represented by the above general formula (1) are more preferably acrylic acid, acryloyloxyethyl succinate, acryloyloxypropyl succinate, 2-carboxyethyl acrylate, and 2-carboxymethyl acrylate.

 ただし、上記カルボキシ基を有するビニル化合物は、一般式(1)で表される化合物に限定されない。上記一般式(1)で表される化合物以外のビニル化合物の例には、マレイン酸、フマル酸、イタコン酸等の不飽和二塩基酸;無水マレイン酸、無水イタコン酸等の不飽和二塩基酸無水物;フマル酸モノメチル、フマル酸モノエチル、マレイン酸モノメチル、マレイン酸モノエチル、シトラコン酸モノメチル、シトラコン酸モノエチル、フタル酸モノメチル、フタル酸モノエチル、イタコン酸モノメチル、イタコン酸モノエチル等の不飽和二塩基酸モノエステル等が含まれる。 However, the vinyl compound having a carboxy group is not limited to the compound represented by general formula (1). Examples of vinyl compounds other than the compound represented by general formula (1) include unsaturated dibasic acids such as maleic acid, fumaric acid, and itaconic acid; unsaturated dibasic acid anhydrides such as maleic anhydride and itaconic anhydride; and unsaturated dibasic acid monoesters such as monomethyl fumarate, monoethyl fumarate, monomethyl maleate, monoethyl maleate, monomethyl citraconate, monoethyl citraconate, monomethyl phthalate, monoethyl phthalate, monomethyl itaconate, and monoethyl itaconate.

 また、フッ化ビニリデン共重合体は、本発明の目的および効果を損なわない範囲で、フッ化ビニリデンおよび上記ビニル化合物以外の化合物(その他の化合物)由来の構成単位を一部に含んでいてもよい。フッ化ビニリデン共重合体は、その他の化合物由来の構成単位を一種のみ含んでいてもよく、二種以上含んでいてもよい。ただし、フッ化ビニリデン共重合体の全構成単位100.0モル%に対する、その他の化合物由来の構成単位の合計量は、10.0モル%以下が好ましく、5.0モル%以下がより好ましい。これらの量は、19F-NMRスペクトルおよびH-NMRスペクトル、中和滴定等から特定される。 Furthermore, the vinylidene fluoride copolymer may partially contain structural units derived from compounds other than vinylidene fluoride and the above vinyl compounds (other compounds) within a range that does not impair the objects and effects of the present invention. The vinylidene fluoride copolymer may contain only one type of structural unit derived from the other compounds, or may contain two or more types. However, the total amount of structural units derived from the other compounds relative to 100.0 mol% of all structural units of the vinylidene fluoride copolymer is preferably 10.0 mol% or less, more preferably 5.0 mol% or less. These amounts are determined from 19F -NMR spectrum, 1H -NMR spectrum, neutralization titration, etc.

 その他の化合物の例には、一分子中にビニル基、およびフッ素原子または含フッ素アルキル基を有する、フッ素系ビニル化合物等が含まれる。フッ素系ビニル化合物の例には、フッ化ビニル;トリフルオロエチレン;テトラフルオロエチレン;クロロトリフルオロエチレン;ヘキサフルオロプロピレン;パーフルオロメチルビニルエーテルに代表されるパーフルオロアルキルビニルエーテル等が含まれる。また、その他の化合物の例には、ビニル基を有し、かつフッ素を含まない化合物も含まれる。その例には、エチレン、プロピレン等の不飽和炭化水素系化合物が含まれる。 Examples of other compounds include fluorine-based vinyl compounds that have a vinyl group and a fluorine atom or a fluorine-containing alkyl group in one molecule. Examples of fluorine-based vinyl compounds include vinyl fluoride; trifluoroethylene; tetrafluoroethylene; chlorotrifluoroethylene; hexafluoropropylene; and perfluoroalkyl vinyl ethers, such as perfluoromethyl vinyl ether. Examples of other compounds also include compounds that have a vinyl group but do not contain fluorine. Examples include unsaturated hydrocarbon compounds such as ethylene and propylene.

 ここで、フッ化ビニリデン共重合体の重量平均分子量Mwaは、上述のように50000以上であればよく、200000以上4000000以下が好ましく、250000以上3000000以下がより好ましい。フッ化ビニリデン共重合体の重量平均分子量Mwaが50000以上であると、電極合剤を用いて得られる電極(電極合剤層)の耐熱性や強度が良好になりやすい。本明細書において、フッ化ビニリデン共重合体の重量平均分子量Mwaはゲルパーミエーションクロマトグラフィー(GPC)によって測定されるポリスチレン換算値である。このとき、溶離液はN,N-ジメチルアセトアミドでとし、重量平均分子量は示差屈折率(RI)検出器によって特定する。Mwaは、3回測定したときの平均値とする。 Here, as mentioned above, the weight-average molecular weight Mwa of the vinylidene fluoride copolymer should be 50,000 or more, preferably 200,000 or more and 4,000,000 or less, and more preferably 250,000 or more and 3,000,000 or less. When the weight-average molecular weight Mwa of the vinylidene fluoride copolymer is 50,000 or more, the heat resistance and strength of the electrode (electrode mixture layer) obtained using the electrode mixture tend to be good. In this specification, the weight-average molecular weight Mwa of the vinylidene fluoride copolymer is a polystyrene-equivalent value measured by gel permeation chromatography (GPC). The eluent used is N,N-dimethylacetamide, and the weight-average molecular weight is determined using a refractive index (RI) detector. Mwa is the average value of three measurements.

 一方、フッ化ビニリデン共重合体中の、カルボキシ基含有共重合体の重量平均分子量Mwcは、上記フッ化ビニリデン共重合体の重量平均分子量Mwaに対して0.90未満、すなわちMwc/Mwa<0.90であればよいが、Mwc/Mwaは0.25以上0.90未満が好ましく、0.25以上0.85以下がより好ましく、0.30以上0.70以下がより好ましく、0.30以上0.60以下がより好ましく、0.30以上0.50以下がより好ましい。上述のように、当該比が0.90未満であると、電極合剤の初期粘度が過度に高まり難くなる。 On the other hand, the weight-average molecular weight Mwc of the carboxyl group-containing copolymer in the vinylidene fluoride copolymer should be less than 0.90 relative to the weight-average molecular weight Mwa of the vinylidene fluoride copolymer, i.e., Mwc/Mwa < 0.90. However, Mwc/Mwa is preferably 0.25 or greater but less than 0.90, more preferably 0.25 or greater but less than 0.85, more preferably 0.30 or greater but less than 0.70, more preferably 0.30 or greater but less than 0.60, and even more preferably 0.30 or greater but less than 0.50. As mentioned above, if this ratio is less than 0.90, the initial viscosity of the electrode mixture is unlikely to increase excessively.

 ここで、カルボキシ基含有共重合体の具体的な重量平均分子量Mwcは、10000以上が好ましく、25000以上4700000以下であることがより好ましく、50000以上3800000以下であることがさらに好ましく、63000以上2800000以下が特に好ましい。カルボキシ基含有共重合体の重量平均分子量Mwcが当該範囲であると、上記比(Mwc/Mwa)が、所望の範囲に収まりやすくなる。 Here, the specific weight average molecular weight Mwc of the carboxy group-containing copolymer is preferably 10,000 or more, more preferably 25,000 or more and 4,700,000 or less, even more preferably 50,000 or more and 3,800,000 or less, and particularly preferably 63,000 or more and 2,800,000 or less. When the weight average molecular weight Mwc of the carboxy group-containing copolymer is within this range, the above ratio (Mwc/Mwa) tends to fall within the desired range.

 本明細書において、上記カルボキシ基含有共重合体の重量平均分子量Mwcは、以下のように測定される値である。フッ化ビニリデン共重合体に、カルボキシ基を標識するための標識物質(1-ブロモメチルピレン)および炭酸カリウムを混合し、カルボキシ基のエステル化を行うことで、ピレンが修飾したフッ化ビニリデン共重合体を得る。そして、紫外・可視(UV-vis)検出器を用い(検出波長は345nm)、溶離液をN,N-ジメチルアセトアミドとしてGPC測定を行ったときの、ポリスチレン換算値である。なお、ピレン構造は紫外・可視域に特徴的な吸収を持ち、、波長345nmの光を強く吸収する。つまり、カルボキシ基を1-ブロモメチルピレンにてエステル化することで、カルボキシ基含有共重合体の重合平均分子量Mwcが特定される。Mwcは、3回測定したときの平均値とする。 In this specification, the weight-average molecular weight Mwc of the carboxyl group-containing copolymer is a value measured as follows. A labeling substance (1-bromomethylpyrene) for labeling the carboxyl groups and potassium carbonate are mixed with a vinylidene fluoride copolymer to esterify the carboxyl groups, resulting in a pyrene-modified vinylidene fluoride copolymer. GPC measurement is then performed using an ultraviolet-visible (UV-visible) detector (detection wavelength: 345 nm) and N,N-dimethylacetamide as the eluent, resulting in a polystyrene-equivalent value. The pyrene structure has characteristic absorption in the ultraviolet-visible region, strongly absorbing light at a wavelength of 345 nm. In other words, the weight-average molecular weight Mwc of the carboxyl group-containing copolymer is determined by esterifying the carboxyl groups with 1-bromomethylpyrene. Mwc is the average of three measurements.

 ここで、上記フッ化ビニリデン共重合体の、インヘレント粘度は、0.5dL/g以上6.0dL/g以下が好ましく、0.5dL/g以上5.0dL/g以下がより好ましく、0.8dL/g以上4.5dL/g以下がさらに好ましい。インヘレント粘度が0.5dL/g以上であると、フッ化ビニリデン共重合体の活物質等や集電体との接着強度が高まりやすい。一方、インヘレント粘度が5.0dL/g以下であると電極合剤の初期粘度が高くなりすぎず、特に作業性に優れやすい。インヘレント粘度(η)は対数粘度を示すものである。まず、フッ化ビニリデン共重合体80mgを20mlのN,N-ジメチルホルムアミドに溶解させて、30℃の恒温槽内でウベローデ粘度計を用いて粘度を測定する。そして、得られた値から、次式に基づいて算出する。
 η=(1/C)・ln(η/η
 上記式において、ηは溶液の粘度、ηは溶媒であるN,N-ジメチルホルムアミド単独の粘度、Cは溶液中のフッ化ビニリデン共重合体の濃度、すなわち0.4g/dlである。
Here, the inherent viscosity of the vinylidene fluoride copolymer is preferably 0.5 dL/g or more and 6.0 dL/g or less, more preferably 0.5 dL/g or more and 5.0 dL/g or less, and even more preferably 0.8 dL/g or more and 4.5 dL/g or less. When the inherent viscosity is 0.5 dL/g or more, the adhesive strength of the vinylidene fluoride copolymer to the active material or current collector tends to be increased. On the other hand, when the inherent viscosity is 5.0 dL/g or less, the initial viscosity of the electrode mixture does not become too high, and workability is particularly excellent. The inherent viscosity (η i ) indicates the logarithmic viscosity. First, 80 mg of vinylidene fluoride copolymer is dissolved in 20 ml of N,N-dimethylformamide, and the viscosity is measured using an Ubbelohde viscometer in a thermostatic bath at 30 °C. Then, the viscosity is calculated from the obtained value based on the following formula.
η i =(1/C)・ln(η/η 0 )
In the above formula, η is the viscosity of the solution, η 0 is the viscosity of the solvent N,N-dimethylformamide alone, and C is the concentration of vinylidene fluoride copolymer in the solution, ie, 0.4 g/dl.

 電極合剤の固形分(合剤層形成時に揮発する成分を除いた成分)中に含まれる、フッ化ビニリデン共重合体の量は、0.2質量%以上20質量%以下が好ましく、0.2質量%以上10質量%以下がより好ましく、0.2質量%以上5質量%以下がさらに好ましい。フッ化ビニリデン共重合体の量が当該範囲であると、強度の高い合剤層が得られやすくなる。 The amount of vinylidene fluoride copolymer contained in the solid content of the electrode mixture (components excluding those that volatilize during mixture layer formation) is preferably 0.2% by mass or more and 20% by mass or less, more preferably 0.2% by mass or more and 10% by mass or less, and even more preferably 0.2% by mass or more and 5% by mass or less. When the amount of vinylidene fluoride copolymer is within this range, a mixture layer with high strength is more likely to be obtained.

 上記フッ化ビニリデン共重合体は、フッ化ビニリデンと、上記カルボキシ基を有するビニル化合物と、必要に応じてその他の化合物を共重合させて調製できる。これらを共重合する方法の例には、懸濁重合、乳化重合、溶液重合等が含まれるが、不純物が少なくなるという観点で懸濁重合が好ましい。 The vinylidene fluoride copolymer can be prepared by copolymerizing vinylidene fluoride with the vinyl compound having a carboxy group, and, if necessary, other compounds. Examples of copolymerization methods include suspension polymerization, emulsion polymerization, and solution polymerization, but suspension polymerization is preferred from the viewpoint of reducing impurities.

 水を分散媒とした懸濁重合においては、メチルセルロース、プロポキシ化メチルセルロース、ヒドロキシエチルセルロース、ヒドロキシプロピルセルロース、ポリビニルアルコール、ポリエチレンオキシド、ゼラチン等の懸濁剤を、共重合に使用する全モノマー(フッ化ビニリデン、カルボキシ基を有するビニル化合物、およびその他のモノマー)100質量部に対して0.005~1.0質量部、好ましくは0.01~0.4質量部の範囲で添加して使用する。 In suspension polymerization using water as the dispersion medium, suspending agents such as methyl cellulose, propoxylated methyl cellulose, hydroxyethyl cellulose, hydroxypropyl cellulose, polyvinyl alcohol, polyethylene oxide, and gelatin are added in an amount of 0.005 to 1.0 part by mass, preferably 0.01 to 0.4 part by mass, per 100 parts by mass of all monomers used in the copolymerization (vinylidene fluoride, vinyl compounds with carboxy groups, and other monomers).

 重合開始剤としては、ジイソプロピルペルオキシジカーボネート、ジノルマルプロピルペルオキシジカーボネート、ジノルマルヘプタフルオロプロピルペルオキシジカーボネート、イソブチリルペルオキサイド、ジ(クロロフルオロアシル)ペルオキサイド、ジ(ペルフルオロアシル)ペルオキサイド、t-ブチルペルオキシピバレート等が使用できる。その使用量は、共重合に使用する全モノマー(フッ化ビニリデン、カルボキシ基を有するビニル化合物、および必要に応じてその他のモノマー)を100質量部とすると、0.05~10質量部、好ましくは0.15~5質量部である。 Polymerization initiators that can be used include diisopropyl peroxydicarbonate, di-normal propyl peroxydicarbonate, di-normal heptafluoropropyl peroxydicarbonate, isobutyryl peroxide, di(chlorofluoroacyl) peroxide, di(perfluoroacyl) peroxide, and t-butyl peroxypivalate. The amount used is 0.05 to 10 parts by mass, preferably 0.15 to 5 parts by mass, based on 100 parts by mass of all monomers used in the copolymerization (vinylidene fluoride, vinyl compound having a carboxy group, and other monomers as needed).

 また、酢酸エチル、酢酸メチル、炭酸ジエチル、アセトン、エタノール、n-プロパノール、アセトアルデヒド、プロピルアルデヒド、プロピオン酸エチル、四塩化炭素等の連鎖移動剤を添加して、得られるフッ化ビニリデン共重合体の重合度を調節することも可能である。連鎖移動剤を使用する場合、その使用量は通常、共重合に使用する全モノマー(フッ化ビニリデン、カルボキシ基を有するビニル化合物、およびどの他のモノマー)を100質量部とすると、0.01~5質量部、好ましくは0.01~3質量部である。 It is also possible to adjust the degree of polymerization of the resulting vinylidene fluoride copolymer by adding a chain transfer agent such as ethyl acetate, methyl acetate, diethyl carbonate, acetone, ethanol, n-propanol, acetaldehyde, propylaldehyde, ethyl propionate, or carbon tetrachloride. When a chain transfer agent is used, the amount used is typically 0.01 to 5 parts by mass, and preferably 0.01 to 3 parts by mass, per 100 parts by mass of all monomers used in the copolymerization (vinylidene fluoride, vinyl compounds having carboxy groups, and any other monomers).

 また、共重合に使用する全モノマー(フッ化ビニリデン、カルボキシ基を有するビニル化合物、およびその他のモノマー)の仕込量は、全モノマー:水の質量比で通常は1:1~1:10、好ましくは1:2~1:5である。 Furthermore, the amount of all monomers (vinylidene fluoride, vinyl compounds having carboxy groups, and other monomers) used in the copolymerization is typically 1:1 to 1:10, preferably 1:2 to 1:5, in terms of the mass ratio of total monomers to water.

 重合温度Tは、重合開始剤の10時間半減期温度T10に応じて適宜選択され、通常はT10-25℃≦T≦T10+25℃の範囲で選択される。例えば、t-ブチルペルオキシピバレートおよびジイソプロピルペルオキシジカーボネートのT10はそれぞれ、54.6℃および40.5℃(日油社製品カタログ参照)である。したがって、t-ブチルペルオキシピバレートおよびジイソプロピルペルオキシジカーボネートを重合開始剤として用いた重合では、その重合温度Tはそれぞれ29.6℃≦T≦79.6℃および15.5℃≦T≦65.5℃の範囲で適宜選択される。重合時間は特に制限されないが、生産性等を考慮すると100時間以下であることが好ましい。重合時の圧力は通常加圧下で行われ、好ましくは2.0~10.0MPa-Gである。 The polymerization temperature T is appropriately selected depending on the 10-hour half-life temperature T10 of the polymerization initiator, and is usually selected within the range of T10 -25°C≦T≦ T10 +25°C. For example, the T10 of t-butyl peroxypivalate and diisopropyl peroxydicarbonate are 54.6°C and 40.5°C, respectively (see NOF Corporation product catalog). Therefore, in polymerizations using t-butyl peroxypivalate and diisopropyl peroxydicarbonate as polymerization initiators, the polymerization temperature T is appropriately selected within the ranges of 29.6°C≦T≦79.6°C and 15.5°C≦T≦65.5°C, respectively. The polymerization time is not particularly limited, but is preferably 100 hours or less in consideration of productivity, etc. The polymerization is usually carried out under increased pressure, preferably 2.0 to 10.0 MPa-G.

 ここで、上記カルボキシ基含有共重合体の重量平均分子量Mwcを、フッ化ビニリデン共重合体の重量平均分子量Mwaに対して、0.90未満とする方法としては、例えば以下の2つの方法が挙げられる。ただし、当該方法に限定されない。第1の方法としては、フッ化ビニリデン(およびその他の化合物)と、カルボキシ基を有するビニル化合物全量とを混合してから重合を開始する方法である。第2の方法としては、フッ化ビニリデン(およびその他の化合物)をある程度重合させてから、反応系にカルボキシ基を有するビニル化合物全量を短時間(例えば2時間以内)で添加し、さらに重合を行う方法である。これにより、重量平均分子量Mwcを所望の範囲にすることができる。また、フッ化ビニリデン共重合体の重量平均分子量Mwaは、重合開始剤量や連鎖移動剤量、重合温度等によって調整可能である。 Here, the following two methods can be used to set the weight-average molecular weight Mwc of the carboxyl group-containing copolymer to less than 0.90 relative to the weight-average molecular weight Mwa of the vinylidene fluoride copolymer. However, these methods are not limited to these. The first method involves mixing vinylidene fluoride (and other compounds) with the entire amount of the vinyl compound having a carboxyl group and then initiating polymerization. The second method involves polymerizing vinylidene fluoride (and other compounds) to a certain extent, then adding the entire amount of the vinyl compound having a carboxyl group to the reaction system within a short period of time (e.g., within two hours), followed by further polymerization. This allows the weight-average molecular weight Mwc to be within the desired range. The weight-average molecular weight Mwa of the vinylidene fluoride copolymer can be adjusted by adjusting the amount of polymerization initiator, the amount of chain transfer agent, the polymerization temperature, etc.

 (活物質)
 本発明の電極合剤が含む活物質は、炭素被覆されたものであって、その炭素被覆量が活物質の質量に対して0.5質量%以上3.0質量%以下である化合物である。炭素被覆量は、各正極材を王水に加熱溶解させ、メンブランフィルターで吸引ろ過し、フィルター上の残量から酸不溶分(炭素量)を算出し特定する。当該炭素被覆量は、0.5質量%以上2.7質量%以下が好ましく、0.5質量%以上2.5質量%以下がより好ましい。
(active material)
The active material contained in the electrode mixture of the present invention is a carbon-coated compound, and the amount of carbon coating is 0.5% by mass or more and 3.0% by mass or less relative to the mass of the active material. The amount of carbon coating is determined by heating and dissolving each positive electrode material in aqua regia, suction filtering through a membrane filter, and calculating the acid-insoluble content (carbon amount) from the amount remaining on the filter. The amount of carbon coating is preferably 0.5% by mass or more and 2.7% by mass or less, and more preferably 0.5% by mass or more and 2.5% by mass or less.

 ここで、上記炭素被覆量を満たす限りにおいて、活物質の種類は特に制限されないが、一般的に、正極活物質であるLiFePO(LFP)やLiFeMnPO(LFMP)等のLiMaPO(ただし、Maは、Co、Ni、Mn、Fe、Mg、Nb、Ti、Al、Zrより選ばれる1種類以上の元素)で表されるオリビン型リチウム化合物では、粒子抵抗低減のために表面が炭素被覆されていることが多く、上記被覆率を満たしやすい。上述のように炭素被覆されている活物質と、カルボキシ基を有する、一般的なフッ化ビニリデン共重合体と混合して電極合剤を調製すると、初期粘度が高まりやすかった。これに対し、上述のフッ化ビニリデン共重合体と組み合わせることで、電極合剤の初期粘度が高まり難い。 Here, the type of active material is not particularly limited as long as the above-mentioned carbon coating amount is satisfied. However, in general, olivine- type lithium compounds represented by LiMaPO4 (where Ma is one or more elements selected from Co, Ni, Mn, Fe, Mg, Nb, Ti, Al, and Zr), such as LiFePO4 ( LFP ) and LiFeMnPO4 (LFMP), which are positive electrode active materials, often have their surfaces carbon-coated to reduce particle resistance, making it easy to satisfy the above-mentioned coverage rate. When an electrode mixture is prepared by mixing the carbon-coated active material as described above with a general vinylidene fluoride copolymer having a carboxy group, the initial viscosity tends to increase. In contrast, when combined with the above-mentioned vinylidene fluoride copolymer, the initial viscosity of the electrode mixture is less likely to increase.

 また、上記LFPやLFMPは、比較的平均粒子径が小さい。電極合剤中の活物質の平均粒子径が小さい場合にも、通常、電極合剤の初期粘度が高まりやすい。ただし、本発明の電極合剤では、上記フッ化ビニリデン共重合体中が活物質を起点として強固なネットワーク構造を形成し難い。したがって、LFPやLFMPの平均粒子径が小さくても、電極合剤の初期粘度が高まり難い。活物質の平均粒子径は、体積基準の粒度累積線図(JISK 1474に準拠)において粒度累積率50%となる粒子径である。活物質の平均粒子径Dv50は、15μm以下とすることができ、例えば0.1μm以上15μm以下とすることができる。ただし、活物質の平均粒子径は当該範囲に限定されない。 Furthermore, the above-mentioned LFP and LFMP have a relatively small average particle diameter. When the average particle diameter of the active material in the electrode mixture is small, the initial viscosity of the electrode mixture is usually likely to increase. However, in the electrode mixture of the present invention, it is difficult for the vinylidene fluoride copolymer to form a strong network structure starting from the active material. Therefore, even if the average particle diameter of LFP or LFMP is small, the initial viscosity of the electrode mixture is unlikely to increase. The average particle diameter of the active material is the particle diameter at which the particle size cumulative ratio is 50% in a volume-based particle size cumulative diagram (based on JIS K 1474). The average particle diameter Dv50 of the active material can be 15 μm or less, for example, 0.1 μm or more and 15 μm or less. However, the average particle diameter of the active material is not limited to this range.

 電極合剤が含む活物質の量は、電極合剤の用途等に応じて適宜選択されるが、電極合剤の固形分の総量に対して、50質量%以上99.9質量%以下が好ましい。活物質の量が当該範囲であると、例えば十分な充放電容量が得られ、電池性能が良好になりやすい。 The amount of active material contained in the electrode mixture is selected appropriately depending on the application of the electrode mixture, but is preferably 50% by mass or more and 99.9% by mass or less of the total solid content of the electrode mixture. When the amount of active material is within this range, for example, sufficient charge/discharge capacity can be obtained, and battery performance is likely to be good.

 (導電助剤)
 電極合剤は、導電助剤をさらに含んでいてもよい。電極合剤が含む導電助剤は、上記活物質同士、または上記活物質と集電体との間の導電性をより高めることができる化合物であれば特に制限されない。導電助剤の例には、アセチレンブラック、ケッチェンブラック、カーボンブラック、黒鉛粉末、カーボンナノファイバー、カーボンナノチューブ、およびカーボンファイバー等が含まれる。
(Conductive additive)
The electrode mixture may further contain a conductive additive. The conductive additive contained in the electrode mixture is not particularly limited as long as it is a compound that can further increase the conductivity between the active materials or between the active material and the current collector. Examples of the conductive additive include acetylene black, ketjen black, carbon black, graphite powder, carbon nanofiber, carbon nanotube, and carbon fiber.

 電極合剤が含む導電助剤の量は、その種類等に応じて適宜選択される。導電性の向上および導電助剤の分散性をともに高める観点から、上記電極合剤の固形分の総量に対して、0.1質量%15質量%以下が好ましく、0.1質量%以上7質量%以下がより好ましく、0.1質量%以上5質量%以下がさらに好ましい。 The amount of conductive additive contained in the electrode mixture is selected appropriately depending on the type of conductive additive. From the perspective of improving both the conductivity and the dispersibility of the conductive additive, the amount is preferably 0.1% to 15% by mass, more preferably 0.1% to 7% by mass, and even more preferably 0.1% to 5% by mass, relative to the total amount of solids in the electrode mixture.

 (溶媒)
 電極合剤は溶媒を含んでいてもよい。溶媒は、非水溶媒であってもよいし、水であってもよい。また、非水溶媒は、極性を有する溶媒(極性溶媒)であってもよい。上記極性溶媒の例には、N,N-ジメチルホルムアミド、N,N-ジメチルアセトアミド、N-メチルピロリドン等のアミド化合物;メタノール、エタノール、イソプロピルアルコール、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、トリプロピレングリコール等のアルコール化合物;o-トルイジン、m-トルイジン、p-トルイジン等のアミン化合物;1-エチル-3-メチルイミダゾリウムビス(トリフルオロメチルスルホニル)イミド等のイミド化合物;γ-ブチロラクトン、δ-ブチロラクトン等のラクトン化合物;ジメチルスルホキシド、スルホラン等のスルホキシド・スルホン化合物;テトラヒドロフラン、ジエチルエーテル、1,4-ジオキサン、ジエチレングリコールジメチルエーテル等のエーテル化合物;アセトン、2-ブタノン、メチルイソブチルケトン、シクロヘキサノン等のケトン化合物等が含まれる。電極合剤は、上記溶媒を1種のみ含んでいてもよく、2種以上含んでいてもよい。
(solvent)
The electrode mixture may contain a solvent. The solvent may be a non-aqueous solvent or water. The non-aqueous solvent may also be a polar solvent (polar solvent). Examples of the polar solvent include amide compounds such as N,N-dimethylformamide, N,N-dimethylacetamide, and N-methylpyrrolidone; alcohol compounds such as methanol, ethanol, isopropyl alcohol, 2-ethyl-1-hexanol, 1-nonanol, lauryl alcohol, and tripropylene glycol; amine compounds such as o-toluidine, m-toluidine, and p-toluidine; imide compounds such as 1-ethyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide; lactone compounds such as γ-butyrolactone and δ-butyrolactone; sulfoxide/sulfone compounds such as dimethyl sulfoxide and sulfolane; ether compounds such as tetrahydrofuran, diethyl ether, 1,4-dioxane, and diethylene glycol dimethyl ether; and ketone compounds such as acetone, 2-butanone, methyl isobutyl ketone, and cyclohexanone. The electrode mixture may contain only one of the above solvents, or may contain two or more of them.

 電極合剤中の溶媒の総量は、特に制限されないが、通常、上述の活物質100質量部に対して10質量部以上150質量部以下が好ましい。 The total amount of solvent in the electrode mixture is not particularly limited, but is typically preferably 10 to 150 parts by weight per 100 parts by weight of the active material.

 (その他の成分)
 電極合剤はさらに、分散剤、接着補助剤、増粘剤等を含んでいてもよく、これらは、公知の化合物を用いることができる。上記分散剤の例としては、ポリビニルピロリドン、メチルセルロース、メトキシ化メチルセルロース、プロポキシ化メチルセルロース、ヒドロキシエチルセルロース、ヒドロキシプロピルセルロース、ポリビニルアルコール、ポリエチレンオキシド、ポリプロピレンオキシド、ゼラチン等が挙げられる。また、上記接着補助剤の例としては、ポリ(メタ)アクリル酸、ポリ(メタ)アクリル酸ナトリウム等のポリ(メタ)アクリル酸金属塩、カルボキシメチルセルロース等が挙げられる。これらの量は、本発明の目的および効果を損なわない範囲であれば特に制限されないが、電極合剤の固形分の総量に対して、15質量%以下が好ましい。
(Other ingredients)
The electrode mixture may further contain a dispersant, an adhesive aid, a thickener, etc., and known compounds can be used for these. Examples of the dispersant include polyvinylpyrrolidone, methylcellulose, methoxylated methylcellulose, propoxylated methylcellulose, hydroxyethyl cellulose, hydroxypropyl cellulose, polyvinyl alcohol, polyethylene oxide, polypropylene oxide, gelatin, etc. Examples of the adhesive aid include poly(meth)acrylic acid, metal salts of poly(meth)acrylic acid such as sodium poly(meth)acrylate, carboxymethyl cellulose, etc. The amount of these is not particularly limited as long as it does not impair the object and effect of the present invention, but is preferably 15 mass% or less based on the total solid content of the electrode mixture.

 また、電極合剤は、リン化合物;硫黄化合物;アミン化合物、およびアンモニウム化合物等の窒素化合物;有機酸;有機エステル;各種シラン系、チタン系およびアルミニウム系のカップリング剤;上述のフッ化ビニリデン共重合体以外のフッ化ビニリデン重合体、ポリテトラフルオロエチレン(PTFE)、スチレン・ブタジエンゴム(SBR)、およびポリアクリロニトリル(PAN)等の樹脂等の添加剤をさらに含んでいてもよい。これらは、本発明の目的および効果を損なわない範囲であれば特に制限されないが、電極合剤の固形分の総量に対して、15質量%以下が好ましい。 The electrode mixture may also contain additives such as phosphorus compounds; sulfur compounds; nitrogen compounds such as amine compounds and ammonium compounds; organic acids; organic esters; various silane-, titanium-, and aluminum-based coupling agents; vinylidene fluoride polymers other than the vinylidene fluoride copolymers mentioned above, and resins such as polytetrafluoroethylene (PTFE), styrene-butadiene rubber (SBR), and polyacrylonitrile (PAN). There are no particular restrictions on these additives as long as they do not impair the objectives and effects of the present invention, but a content of 15% by mass or less of the total solid content of the electrode mixture is preferred.

 (電極合剤の物性)
 電極合剤の粘度は、電極合剤を塗工して合剤層を形成するときの液だれ・塗工ムラ・塗工後の乾燥遅延を防止でき、合剤層作製時の作業性や塗布性が良好な粘度であれば特に限定されない。当該電極合剤のE型粘度計により25℃で測定される値であり、E型粘度計で25℃、60秒間の保温期間を置いてから、せん断速度1s-1でローターを回転させ、ローター回転開始から120秒後に測定される値は、2000mPa・s以上60000mPa・s以下が好ましく、5000mPa・s以上30000mPa・s以下がより好ましい。初期粘度が当該範囲であると、合剤層を形成するときの取扱性がさらに良好になりやすい。
(Physical properties of electrode mixture)
The viscosity of the electrode mixture is not particularly limited as long as it can prevent dripping, uneven coating, and delayed drying after coating when applying the electrode mixture to form a mixture layer, and provides good workability and applicability when preparing the mixture layer. The value of the electrode mixture measured at 25 ° C. using an E-type viscometer is measured after a 60-second incubation period at 25 ° C., rotating the rotor at a shear rate of 1 s −1 , and measuring 120 seconds after the start of rotor rotation. The value is preferably 2000 mPa s or more and 60,000 mPa s or less, more preferably 5,000 mPa s or more and 30,000 mPa s or less. When the initial viscosity is within this range, handling when forming the mixture layer tends to be even better.

 また、E型粘度計で25℃、60秒間の保温期間を置いてから、せん断速度40s-1でローターを回転させ、ローター回転開始から30秒後に測定される値は、1000mPa・s以上5000mPa・s以下が好ましく、1000mPa・s以上4000mPa・s以下がより好ましい。さらに、せん断速度40s-1で特定される粘度と、せん断速度1s-1で特定される粘度との比、すなわち(せん断速度1s-1で特定される粘度/せん断速度40s-1で特定される粘度)は、2以上12以下であることが好ましく、3以上11以下であることがより好ましい。上記比が当該範囲であると、合剤層を形成するときの電極合剤の取扱性がさらに良好になりやすい。 Furthermore, after a 60-second incubation period at 25 ° C. using an E-type viscometer, the rotor is rotated at a shear rate of 40 s -1 , and the value measured 30 seconds after the start of rotor rotation is preferably 1000 mPa · s or more and 5000 mPa · s or less, more preferably 1000 mPa · s or more and 4000 mPa · s or less. Furthermore, the ratio of the viscosity specified at a shear rate of 40 s -1 to the viscosity specified at a shear rate of 1 s -1 , i.e., (viscosity specified at a shear rate of 1 s -1 / viscosity specified at a shear rate of 40 s -1 ), is preferably 2 or more and 12 or less, more preferably 3 or more and 11 or less. When the ratio is within this range, the handleability of the electrode mixture when forming the mixture layer tends to be further improved.

 (電極合剤の調製方法)
 上記電極合剤は、全ての成分を一度に混合して調製してもよく、一部の成分を先に混合し、後から残りの成分を混合して調製してもよい。
(Method for preparing electrode mixture)
The electrode mixture may be prepared by mixing all of the components at once, or by first mixing some of the components and then mixing the remaining components.

 2.電極
 上述の電極合剤は、各種非水電解質二次電池の電極の合剤層の形成に使用できる。非水電解質二次電池の電極は、例えば、集電体と、当該集電体上に配置された合剤層とを含む。当該合剤層の形成に、上述の電極合剤を用いることができる。
2. Electrode The above-described electrode mixture can be used to form a mixture layer of an electrode of various non-aqueous electrolyte secondary batteries. An electrode of a non-aqueous electrolyte secondary battery includes, for example, a current collector and a mixture layer disposed on the current collector. The above-described electrode mixture can be used to form the mixture layer.

 ・集電体
 集電体は、電気を取り出すための端子である。集電体の材質としては、特に限定されるものではなく、アルミニウム、銅、鉄、ステンレス鋼、鋼、ニッケル、チタン等の金属箔あるいは金属網等、またはその表面にカーボンブラック等を含む層を形成したものを用いることができる。また、他の媒体の表面にカーボンブラック等を含む層を形成したものや、上記金属箔あるいは金属網等を施したものであってもよい。
Current Collector The current collector is a terminal for extracting electricity. The material of the current collector is not particularly limited, and metal foil or metal mesh of aluminum, copper, iron, stainless steel, steel, nickel, titanium, etc., or a layer containing carbon black or the like formed on the surface thereof can be used. Alternatively, the current collector may be a medium having a layer containing carbon black or the like formed on the surface thereof, or a medium having the above-mentioned metal foil or metal mesh applied thereto.

 ・合剤層
 合剤層は、上述の電極合剤を集電体上に塗布し、固化させた層である。すなわち、合剤層は、上述のフッ化ビニリデン系化合物および活物質を少なくとも含む。合剤層は、上記集電体の一方の面のみに形成されていてもよく、両方の面に配置されていてもよい。
The mixture layer is a layer formed by applying the electrode mixture described above onto a current collector and solidifying it. That is, the mixture layer contains at least the vinylidene fluoride compound and the active material described above. The mixture layer may be formed on only one surface of the current collector, or may be disposed on both surfaces.

 合剤層は、上述の電極合剤が含む成分、すなわちフッ化ビニリデン共重合体および活物質を少なくとも含み、必要に応じて導電助剤や、分散剤、接着補助剤、増粘剤等の各種添加剤等をさらに含む。これらは、電極合剤で説明したものと同様である。 The mixture layer contains at least the components contained in the electrode mixture described above, namely vinylidene fluoride copolymer and active material, and may further contain various additives such as a conductive aid, dispersant, adhesive aid, and thickener as needed. These are the same as those described for the electrode mixture.

 ここで、合剤層の厚みは特に限定されるものではないが、一例において、1μm以上300μm以下が好ましい。また、集電体の一方の面に形成された合剤層の目付量は、特に限定されるものではなく、任意の目付量とすることができるが、一例において、50g/m以上500g/m以下が好ましく、100g/m以上300g/m以下がより好ましい。 The thickness of the mixture layer is not particularly limited, but is preferably 1 μm or more and 300 μm or less, for example. The basis weight of the mixture layer formed on one surface of the current collector is not particularly limited, and can be any basis weight, but is preferably 50 g/ m2 or more and 500 g/m2 or less , and more preferably 100 g/m2 or more and 300 g/m2 or less , for example.

 上記合剤層は、上述の電極合剤を集電体上に塗布する工程と、これを固化させる工程と、を行うことで形成できる。 The mixture layer can be formed by applying the electrode mixture described above to a current collector and then solidifying it.

 電極合剤の塗布方法は、特に限定されず、ドクターブレード法、リバースロール法、コンマバー法、グラビヤ法、エアーナイフ法、ダイコート法およびディップコート法等を適用できる。 The method for applying the electrode mixture is not particularly limited, and methods such as the doctor blade method, reverse roll method, comma bar method, gravure method, air knife method, die coating method, and dip coating method can be used.

 また、電極合剤の塗布後、任意の温度で加熱し、溶媒を乾燥させる。乾燥温度は、一例において、60℃以上200℃以下が好ましく、80℃以上150℃以下がより好ましい。加熱は、異なる温度で複数回行ってもよい。なお、大気圧下、加圧下、減圧下で合剤中の溶媒を乾燥させてもよいし、空気、窒素、アルゴン等の環境下で乾燥させてもよい。乾燥後にさらに熱処理を行ってもよい。 Furthermore, after application of the electrode mixture, it is heated at a desired temperature to dry the solvent. In one example, the drying temperature is preferably 60°C or higher and 200°C or lower, and more preferably 80°C or higher and 150°C or lower. Heating may be performed multiple times at different temperatures. The solvent in the mixture may be dried under atmospheric pressure, increased pressure, or reduced pressure, or may be dried in an environment such as air, nitrogen, or argon. A further heat treatment may be performed after drying.

 上記電極合剤の塗布および乾燥後、さらにプレス処理を行ってもよい。プレス処理を行うことにより、電極密度を向上させることができる。プレス圧力は、一例において、1kPa以上10GPa以下が好ましい。 After the electrode mixture has been applied and dried, a pressing process may be performed. Pressing can improve electrode density. In one example, the pressing pressure is preferably 1 kPa or more and 10 GPa or less.

 3.電池
 上述の電極合剤は、上述のように、各種非水電解質二次電池等の電極に使用可能であるが、非水電解質二次電池の他の層の形成に使用してもよい。
3. Batteries As described above, the electrode mixture described above can be used in electrodes of various non-aqueous electrolyte secondary batteries, etc., but it may also be used to form other layers of non-aqueous electrolyte secondary batteries.

 以下、本発明の具体的な実施例を比較例とともに説明するが、本発明はこれらに限定されるものではない。 Specific examples of the present invention will be described below along with comparative examples, but the present invention is not limited to these.

 1.各種物性の測定方法および評価方法
 フッ化ビニリデン共重合体のインヘレント粘度、フッ化ビニリデン共重合体の重量平均分子量Mwa、およびカルボキシ基含有共重合体の重量平均分子量Mwcを以下に示す。 電極活物質の平均粒子径(Dv50)および炭素被覆量の測定法方法を以下示す。
 さらに、電極合剤のスラリー粘度の測定方法を以下に示す。
1. Measurement and evaluation methods for various physical properties The inherent viscosity of the vinylidene fluoride copolymer, the weight average molecular weight Mwa of the vinylidene fluoride copolymer, and the weight average molecular weight Mwc of the carboxy group-containing copolymer are shown below. The measurement methods for the average particle size (Dv50) and carbon coating amount of the electrode active material are shown below.
Furthermore, the method for measuring the slurry viscosity of the electrode mixture is shown below.

 (1)フッ化ビニリデン共重合体のインヘレント粘度
 フッ化ビニリデン共重合体のインヘレント粘度は、以下のように測定した。まず、フッ化ビニリデン共重合体80mgを20mlのN,N-ジメチルホルムアミドに溶解させて、30℃の恒温槽内でウベローデ粘度計を用いて粘度を測定した。そして、得られた値から、次式に基づいて、フッ化ビニリデン共重合体のインヘレント粘度(η)を算出した。
 η=(1/C)・ln(η/η
 上記式において、ηは溶液の粘度、ηは溶媒であるN,N-ジメチルホルムアミド単独の粘度、Cは溶液中のフッ化ビニリデン系重合体の濃度、すなわち0.4g/dlである。
(1) Inherent Viscosity of Vinylidene Fluoride Copolymer The inherent viscosity of the vinylidene fluoride copolymer was measured as follows. First, 80 mg of the vinylidene fluoride copolymer was dissolved in 20 ml of N,N-dimethylformamide, and the viscosity was measured using an Ubbelohde viscometer in a thermostatic bath at 30° C. Then, the inherent viscosity (η i ) of the vinylidene fluoride copolymer was calculated from the obtained value according to the following formula.
η i =(1/C)・ln(η/η 0 )
In the above formula, η is the viscosity of the solution, η 0 is the viscosity of the solvent N,N-dimethylformamide alone, and C is the concentration of the vinylidene fluoride polymer in the solution, ie, 0.4 g/dl.

 (2)フッ化ビニリデン共重合体の重量平均分子量Mwa
 各実施例および比較例で調製したフッ化ビニリデン共重合体の重量平均分子量Mw1は、示差屈折計(RI)で測定した。具体的には、以下の条件でGPC(ゲルパーミエーション測定)を行い、示差屈折率検出器でMwaを求めた。これを3回行い、その平均値をMwaとした。
 分離カラム:Shodex KD-807、KD-806M
 検出器:日本分光社製RI-4030(示差屈折率検出器)
 溶離液:濃度10mMのLiBr-N,N-ジメチルアセトアミド(DMAc)溶液
 溶離液の流速:0.5mL/min
 カラム温度:40℃
 検量線用の標準ポリマー:TSK standard POLY(STYRENE)(標準ポリスチレン)(東ソー社製)
(2) Weight average molecular weight Mwa of vinylidene fluoride copolymer
The weight-average molecular weight Mw1 of the vinylidene fluoride copolymer prepared in each Example and Comparative Example was measured using a differential refractometer (RI). Specifically, GPC (gel permeation chromatography) was performed under the following conditions, and Mwa was determined using a differential refractive index detector. This was performed three times, and the average value was taken as Mwa.
Separation column: Shodex KD-807, KD-806M
Detector: JASCO RI-4030 (differential refractive index detector)
Eluent: 10 mM LiBr-N,N-dimethylacetamide (DMAc) solution Eluent flow rate: 0.5 mL/min
Column temperature: 40°C
Standard polymer for calibration curve: TSK standard POLY(STYRENE) (standard polystyrene) (manufactured by Tosoh Corporation)

 (3)カルボキシ基含有共重合体の重量平均分子量Mwc
 DMAc10mgに各実施例および比較例で調製したフッ化ビニリデン共重合体10mg、1-ブロモメチルピレン2mg、炭酸カリウム2mgを加え、50℃の恒温振とう槽にて攪拌しながら、溶解・反応を行い、0.45μmのフィルターにて炭酸カリウムを除去した。これにより、フッ化ビニリデン共重合体中のカルボキシ基含有共重合体のカルボキシ基を1-ブロモメチルピレンで標識した。
(3) Weight average molecular weight Mwc of carboxy group-containing copolymer
To 10 mg of DMAc were added 10 mg of vinylidene fluoride copolymer prepared in each Example and Comparative Example, 2 mg of 1-bromomethylpyrene, and 2 mg of potassium carbonate, and the mixture was dissolved and reacted while stirring in a thermostatic shaking bath at 50°C, and the potassium carbonate was removed using a 0.45 μm filter. As a result, the carboxy group of the carboxy group-containing copolymer in the vinylidene fluoride copolymer was labeled with 1-bromomethylpyrene.

 1-ブロモメチルピレンで標識したフッ化ビニリデン共重合体が含む、カルボキシ基含有共重合体(波長345nmの光を吸収する重合体)の重量平均分子量を、UV-vis検出器にて特定した。検出器以外は上記のMwaと同じ測定条件で実施した。検出波長は345nmとし、カルボキシ基含有共重合体の重量平均分子量Mwcを求めた。これを3回行い、その平均値をMwcとした。 The weight-average molecular weight of the carboxyl group-containing copolymer (a polymer that absorbs light at a wavelength of 345 nm) contained in the vinylidene fluoride copolymer labeled with 1-bromomethylpyrene was determined using a UV-vis detector. The measurement was carried out under the same conditions as for Mwa above, except for the detector. The detection wavelength was 345 nm, and the weight-average molecular weight Mwc of the carboxyl group-containing copolymer was determined. This was carried out three times, and the average value was taken as Mwc.

 (4)電極活物質の平均粒子径Dv50測定
 各電極活物質0.01gに対し、分散剤(カチオン系界面活性剤「SNウェット366」(サンノプコ社製))0.1gを加え、試料に分散剤を馴染ませた。次に、純水20mLを加え、超音波洗浄機で約5分間分散させた後、粒径分布測定装置(マイクロトラック社製:MT3300EXII)で、粒子径0.1~1000μmの範囲における粒径分布を求めた。なお、分散媒は純水とし、分散媒の屈折率は1.333とした。得られた粒径分布から、累積度数が体積基準で50%となる粒子径算出し、平均粒子径Dv50を求めた。
(4) Measurement of Average Particle Diameter Dv50 of Electrode Active Material 0.1 g of dispersant (cationic surfactant "SN Wet 366" (manufactured by San Nopco)) was added to 0.01 g of each electrode active material, and the dispersant was allowed to soak into the sample. Next, 20 mL of pure water was added, and the mixture was dispersed in an ultrasonic cleaner for approximately 5 minutes. The particle size distribution in the particle diameter range of 0.1 to 1000 μm was determined using a particle size distribution measuring device (manufactured by Microtrac: MT3300EXII). The dispersion medium was pure water, and the refractive index of the dispersion medium was 1.333. From the obtained particle size distribution, the particle diameter at which the cumulative frequency was 50% on a volume basis was calculated, and the average particle diameter Dv50 was determined.

 (5)電極活物質の炭素被覆量の特定方法
 各電極活物質500mgをビーカーに秤量し、水40mLと王水(硝酸3mL+塩酸9mL)を加えて加熱溶解後、メンブランフィルターで吸引ろ過し、残量から酸不溶分(炭素被覆量)を算出した
(5) Method for Determining the Amount of Carbon Coating on Electrode Active Material 500 mg of each electrode active material was weighed into a beaker, 40 mL of water and aqua regia (3 mL of nitric acid + 9 mL of hydrochloric acid) were added, and the mixture was dissolved by heating. The mixture was then suction filtered through a membrane filter, and the acid-insoluble portion (amount of carbon coating) was calculated from the remaining amount.

 (6)電極合剤のスラリー粘度
 実施例および比較例で調製した電極合剤のスラリー粘度を測定した。電極合剤は、調製直後の電極合剤をE型粘度計(東機産業社製RE-215形粘度計、ローター3°×R14)の装置内に仕込んだ。当該装置内にて25℃、60秒間の保温期間を置いてから、せん断速度1s-1でローターを回転させ、ローター回転開始から120秒後の粘度をスラリー粘度として特定した。
 さらに、上記装置内にて、25℃、60秒間の保温期間を置いてから、せん断速度40s-1でローターを回転させ、ローター回転開始から30秒後の粘度をスラリー粘度として特定した。
 また、特定したせん断速度1s-1のスラリー粘度と、せん断速度40s-1のスラリー粘度との粘度比(せん断速度1s-1のスラリー粘度/せん断速度40s-1のスラリー粘度)を特定した。
(6) Slurry viscosity of electrode mixture The slurry viscosity of the electrode mixture prepared in the examples and comparative examples was measured. The electrode mixture was placed in an E-type viscometer (RE-215 type viscometer manufactured by Toki Sangyo Co., Ltd., rotor 3° × R14) immediately after preparation. After a 60-second incubation period at 25°C in the apparatus, the rotor was rotated at a shear rate of 1 s -1 , and the viscosity 120 seconds after the start of rotor rotation was determined as the slurry viscosity.
After the device was left to incubate at 25° C. for 60 seconds, the rotor was rotated at a shear rate of 40 s −1 , and the viscosity 30 seconds after the rotor started to rotate was determined as the slurry viscosity.
Also, the viscosity ratio of the specified slurry viscosity at a shear rate of 1 s −1 to the slurry viscosity at a shear rate of 40 s −1 (slurry viscosity at a shear rate of 1 s −1 /slurry viscosity at a shear rate of 40 s −1 ) was specified.

 2.材料の準備
 実施例および比較例で調製する電極合剤の材料として、以下のものを準備した。
2. Preparation of Materials The following materials were prepared as electrode mixtures for the Examples and Comparative Examples.

 (1)活物質
 ・LFP-A 炭素被覆量:1.0%、平均粒子径D50:2μm)
 ・LFP-B 炭素被覆量:1.4%、平均粒子径D50:4μm)
 ・LFP-C 炭素被覆量:2.1%、平均粒子径D50:10μm)
 ・LFMP 、炭素被覆量:2.0%、平均粒子径D50:1μm)
 ・LCO 炭素被覆量:0.0%、平均粒子径D50:2μm)
(1) Active material ・LFP-A Carbon coverage: 1.0%, average particle diameter D50: 2 μm)
・LFP-B Carbon coverage: 1.4%, average particle diameter D50: 4 μm)
・LFP-C Carbon coverage: 2.1%, average particle diameter D50: 10 μm)
LFMP, carbon coating amount: 2.0%, average particle size D50: 1 μm)
・LCO carbon coverage: 0.0%, average particle diameter D50: 2 μm)

 (2)フッ化ビニリデン共重合体
 ・VDF/APS-1:下記合成例1で調製
 ・VDF/APS-2:下記合成例2で調
 ・VDF/AA-1:下記合成例3で調製
 ・VDF/AA-2:下記合成例4で調製
(2) Vinylidene fluoride copolymers VDF/APS-1: Prepared in Synthesis Example 1 below VDF/APS-2: Prepared in Synthesis Example 2 below VDF/AA-1: Prepared in Synthesis Example 3 below VDF/AA-2: Prepared in Synthesis Example 4 below

 <合成例1>
 内容量2リットルのオートクレーブに分散媒としてイオン交換水を1240g、セルロース系懸濁剤としてメトローズSM-100(信越化学工業社製)を0.4g、アクリロイロキシプロピルコハク酸(APS)を2.0g、重合開始剤の濃度が50wt%であるジイソプロピルパーオキシジカーボネート-HFE-347pc-f溶液を1.40g、連鎖移動剤として酢酸エチルを0.8g、フッ化ビニリデンを400g仕込み、45℃まで2時間かけて昇温した。温度を45℃に維持しながら、系内の圧力が1.5MPaまで低下するまで反応を続けた。
 重合終了後、重合体スラリーを、95℃で60分間熱処理した後、脱水し、水洗して更に80℃で20時間乾燥させることにより、フッ化ビニリデン(VDF)とアクリロイロキシプロピルコハク酸(APS)との共重合である、フッ化ビニリデン共重合体(VDF/APS-1)の粉末を得た。当該フッ化ビニリデン共重合体のインヘレント粘度、重量平均分子量Mwa、および含有するカルボキシ基含有共重合体の重量平均分子量Mwcを下記表1に示す。
<Synthesis Example 1>
A 2-liter autoclave was charged with 1,240 g of ion-exchanged water as a dispersion medium, 0.4 g of Metrolose SM-100 (manufactured by Shin-Etsu Chemical Co., Ltd.) as a cellulose-based suspension agent, 2.0 g of acryloyloxypropyl succinic acid (APS), 1.40 g of a diisopropyl peroxydicarbonate-HFE-347pc-f solution having a polymerization initiator concentration of 50 wt %, 0.8 g of ethyl acetate as a chain transfer agent, and 400 g of vinylidene fluoride, and the temperature was raised to 45°C over 2 hours. While maintaining the temperature at 45°C, the reaction was continued until the pressure in the system decreased to 1.5 MPa.
After the polymerization was completed, the polymer slurry was heat-treated at 95°C for 60 minutes, dehydrated, washed with water, and further dried at 80°C for 20 hours to obtain a powder of vinylidene fluoride copolymer (VDF/APS-1), which is a copolymer of vinylidene fluoride (VDF) and acryloyloxypropyl succinic acid (APS). The inherent viscosity, weight-average molecular weight Mwa, and weight-average molecular weight Mwc of the carboxy group-containing copolymer contained in the vinylidene fluoride copolymer are shown in Table 1 below.

 <合成例2>
 内容量2リットルのオートクレーブに分散媒としてイオン交換水を1054.5g、セルロース系懸濁剤としてメトローズSM-100(信越化学工業社製)を0.23g、APSを0.07g、重合開始剤の濃度が50wt%であるジイソプロピルパーオキシジカーボネート-HFE-347pc-f溶液を3.50g、フッ化ビニリデンを400g仕込み、26℃まで55分間かけて昇温した。温度を26℃に維持しながら、昇温開始2時間後から濃度が5wt%であるAPS水溶液を4.3時間かけて溶質換算で0.86g添加した。昇温終了時の圧力から0.2MPaG低下した時点から、55℃まで40分間かけて昇温した。温度を55℃に維持しながら、系内の圧力が1.3MPaGまで低下するまで反応を続けた。
 得られた重合体スラリーを合成例1と同様の方法で処理することで、フッ化ビニリデン(VDF)とアクリロイロキシプロピルコハク酸(APS)との共重合である、フッ化ビニリデン共重合体(VDF/APS-2)の粉末を得た。当該フッ化ビニリデン共重合体のインヘレント粘度、重量平均分子量Mwa、および含有するカルボキシ基含有共重合体の重量平均分子量Mwcを下記表1に示す。
<Synthesis Example 2>
A 2-liter autoclave was charged with 1054.5 g of ion-exchanged water as a dispersion medium, 0.23 g of Metrose SM-100 (manufactured by Shin-Etsu Chemical Co., Ltd.) as a cellulose-based suspending agent, 0.07 g of APS, 3.50 g of diisopropyl peroxydicarbonate-HFE-347pc-f solution having a polymerization initiator concentration of 50 wt%, and 400 g of vinylidene fluoride, and the mixture was heated to 26°C over 55 minutes. While maintaining the temperature at 26°C, 2 hours after the start of the temperature increase, 0.86 g of an aqueous APS solution having a concentration of 5 wt% was added over 4.3 hours in solute equivalent. From the point when the pressure had decreased by 0.2 MPaG from the pressure at the end of the temperature increase, the mixture was heated to 55°C over 40 minutes. While maintaining the temperature at 55°C, the reaction was continued until the pressure in the system decreased to 1.3 MPaG.
The obtained polymer slurry was treated in the same manner as in Synthesis Example 1 to obtain a powder of vinylidene fluoride copolymer (VDF/APS-2), which is a copolymer of vinylidene fluoride (VDF) and acryloyloxypropyl succinic acid (APS). The inherent viscosity, weight average molecular weight Mwa, and weight average molecular weight Mwc of the carboxy group-containing copolymer contained therein are shown in Table 1 below.

 <合成例3>
 内容量2リットルのオートクレーブに分散媒としてイオン交換水を1056g、セルロース系懸濁剤としてメトローズSM-100(信越化学工業社製)を0.44g、アクリル酸(AA)を9.37g、重合開始剤の濃度が50wt%であるターシャリーブチルパーオキシピバレート-HFE-347pc-f溶液を5.28g、連鎖移動剤として酢酸エチルを0.44g、フッ化ビニリデンを440g仕込み、52℃まで110分間かけて昇温した。温度を52℃に維持しながら、系内の圧力が4.7MPaGまで低下するまで反応を続けた。
 得られた重合体スラリーを合成例1と同様の方法で処理することで、フッ化ビニリデン(VDF)とアクリル酸(AA)との共重合である、フッ化ビニリデン共重合体(VDF/AA-1)の粉末を得た。当該フッ化ビニリデン共重合体のインヘレント粘度、重量平均分子量Mwa、および含有するカルボキシ基含有共重合体の重量平均分子量Mwcを下記表1に示す。
<Synthesis Example 3>
A 2-liter autoclave was charged with 1,056 g of ion-exchanged water as a dispersion medium, 0.44 g of Metrose SM-100 (manufactured by Shin-Etsu Chemical Co., Ltd.) as a cellulose-based suspension agent, 9.37 g of acrylic acid (AA), 5.28 g of a tertiary butyl peroxypivalate-HFE-347pc-f solution having a polymerization initiator concentration of 50 wt %, 0.44 g of ethyl acetate as a chain transfer agent, and 440 g of vinylidene fluoride, and the temperature was raised to 52°C over 110 minutes. While maintaining the temperature at 52°C, the reaction was continued until the pressure in the system decreased to 4.7 MPaG.
The resulting polymer slurry was treated in the same manner as in Synthesis Example 1 to obtain a powder of vinylidene fluoride copolymer (VDF/AA-1), which is a copolymer of vinylidene fluoride (VDF) and acrylic acid (AA). The inherent viscosity, weight average molecular weight Mwa, and weight average molecular weight Mwc of the carboxy group-containing copolymer contained in the vinylidene fluoride copolymer are shown in Table 1 below.

 <合成例4>
 内容量2リットルのオートクレーブに分散媒としてイオン交換水を1056g、セルロース系懸濁剤としてメトローズSM-100(信越化学工業社製)を0.44g、アクリル酸(AA)を0.22g、重合開始剤の濃度が50wt%であるターシャリーブチルパーオキシピバレート-HFE-347pc-f溶液を3.08g、連鎖移動剤としてイソドデカンを0.44g、フッ化ビニリデンを440g仕込み、52℃まで110分間かけて昇温した。温度を52℃に維持しながら、昇温終了直後の圧力を維持するように1wt%のAA水溶液を溶質換算で3.74g添加した。系内の圧力が7.18MPaGまで低下するまで反応を続けた。
 得られた重合体スラリーを合成例1と同様の方法で処理することで、フッ化ビニリデン(VDF)とアクリル酸(AA)との共重合である、フッ化ビニリデン共重合体(VDF/AA-2)の粉末を得た。当該フッ化ビニリデン共重合体のインヘレント粘度、重量平均分子量Mwa、および含有するカルボキシ基含有共重合体の重量平均分子量Mwcを下記表1に示す。
<Synthesis Example 4>
A 2-liter autoclave was charged with 1,056 g of ion-exchanged water as a dispersion medium, 0.44 g of Metrose SM-100 (manufactured by Shin-Etsu Chemical Co., Ltd.) as a cellulose-based suspension agent, 0.22 g of acrylic acid (AA), 3.08 g of a tertiary butyl peroxypivalate-HFE-347pc-f solution having a polymerization initiator concentration of 50 wt%, 0.44 g of isododecane as a chain transfer agent, and 440 g of vinylidene fluoride, and the temperature was raised to 52°C over 110 minutes. While maintaining the temperature at 52°C, 3.74 g of a 1 wt% AA aqueous solution (in terms of solute) was added so as to maintain the pressure immediately after completion of the temperature increase. The reaction was continued until the pressure in the system decreased to 7.18 MPaG.
The resulting polymer slurry was treated in the same manner as in Synthesis Example 1 to obtain a powder of vinylidene fluoride copolymer (VDF/AA-2), which is a copolymer of vinylidene fluoride (VDF) and acrylic acid (AA). The inherent viscosity, weight average molecular weight Mwa, and weight average molecular weight Mwc of the carboxy group-containing copolymer contained in the vinylidene fluoride copolymer are shown in Table 1 below.

 (3)フッ化ビニリデン共重合体の物性
 フッ化ビニリデン共重合体の物性を以下に示す。
(3) Physical Properties of Vinylidene Fluoride Copolymer The physical properties of the vinylidene fluoride copolymer are shown below.

 3.電極合剤の調製
 以下の方法で、各電極合剤を調製した。
3. Preparation of electrode mixtures Each electrode mixture was prepared by the following method.

 (実施例1)
 電極活物質としてLFP:Aを使用し、フッ化ビニリデン共重合体(バインダー)としてVDF/APS-1を使用し、導電助剤としてカーボンナノチューブ(CNT)NMP分散液を使用した。そして、遊星式自転公転ミキサー、シンキー社製、あわとり練太郎ARE310を用いこれらを混合し、電極合剤を調製した。得られた電極合剤における、電極活物質、導電助剤、およびバインダーの質量比は100:2:2.5であり、固形分濃度は55.0質量%であった。このときのスラリー粘度を表2に示す。
Example 1
LFP:A was used as the electrode active material, VDF/APS-1 was used as the vinylidene fluoride copolymer (binder), and a carbon nanotube (CNT) NMP dispersion was used as the conductive additive. These were then mixed using a planetary centrifugal mixer, Thinky Mixer ARE310, to prepare an electrode mixture. The mass ratio of the electrode active material, conductive additive, and binder in the resulting electrode mixture was 100:2:2.5, and the solids concentration was 55.0 mass%. The slurry viscosity at this time is shown in Table 2.

 (実施例2~5、比較例1~5、および参考例1、2)
 表2に示すように、電極活物質の種類、フッ化ビニリデン共重合体の種類、実施例4、比較例4の固形分濃度52%に変更した以外は、上記実施例1と同様に電極合剤を調製した。
(Examples 2 to 5, Comparative Examples 1 to 5, and Reference Examples 1 and 2)
As shown in Table 2, electrode mixtures were prepared in the same manner as in Example 1 above, except that the type of electrode active material, the type of vinylidene fluoride copolymer, and the solid content concentration in Example 4 and Comparative Example 4 were changed to 52%.

 (結果)
(result)

 上記表2に示すように、炭素によって被覆されていない活物質を用いた場合には、カルボキシ基を有するフッ化ビニリデン共重合体の相違によって、大きな差はなかった(参考例1および参考例2)。これに対し、実施例1および比較例1を比較すると、同一の活物質を用いたとしても、上記Mwc/Mwaの違いによって、スラリー粘度(特にせん断速度s-1の場合)に大きな差があり、さらに粘度比にも大きな差があった。実施例2~5、および比較例2~5の比較においても、同様である。そして、フッ化ビニリデン共重合体の重量平均分子量Mwaが50000以上であり、かつカルボキシ基含有共重合体の重量平均分子量Mwcが、Mwaに対して0.90未満であると、スラリー粘度(特にせん断速度s-1)が51041mPa・s以下となり、さらに粘度比も11.2以下であった(実施例1~5)。つまり、参考例1および参考例2と大きな差がなかった。 As shown in Table 2 above, when an active material not coated with carbon was used, there was no significant difference depending on the vinylidene fluoride copolymer having a carboxy group (Reference Examples 1 and 2). In contrast, when Example 1 and Comparative Example 1 were compared, even when the same active material was used, there was a significant difference in the slurry viscosity (particularly at a shear rate of s −1 ) and also in the viscosity ratio depending on the Mwc/Mwa ratio. This was also the case when Examples 2 to 5 and Comparative Examples 2 to 5 were compared. Furthermore, when the weight-average molecular weight Mwa of the vinylidene fluoride copolymer was 50,000 or more and the weight-average molecular weight Mwc of the carboxy group-containing copolymer was less than 0.90 relative to Mwa, the slurry viscosity (particularly at a shear rate of s −1 ) was 51,041 mPa·s or less, and the viscosity ratio was also 11.2 or less (Examples 1 to 5). In other words, there was no significant difference from Reference Examples 1 and 2.

 本出願は、2024年3月29日出願の特願2024-056545号に基づく優先権を主張する。当該出願明細書に記載された内容は、すべて本願明細書に援用される。 This application claims priority from Japanese Patent Application No. 2024-056545, filed March 29, 2024. The entire contents of the specification of that application are incorporated herein by reference.

 本発明によれば、炭素で被覆された電極活物質、およびカルボキシ基を有するフッ化ビニリデン共重合体を含み、初期粘度が低く、かつ取扱性が良好な電極合剤が提供される。当該電極合剤は、各種電池の製造分野において、非常に有用である。
 
According to the present invention, there is provided an electrode mixture that contains a carbon-coated electrode active material and a vinylidene fluoride copolymer having a carboxy group, has a low initial viscosity, and is easy to handle. The electrode mixture is very useful in the field of manufacturing various batteries.

Claims (8)

 フッ化ビニリデン由来の構成単位、およびカルボキシ基を有するビニル化合物由来の構成単位、を有するフッ化ビニリデン共重合体と、
 炭素で被覆された電極活物質と、
 を含む電極合剤であり、
 前記電極活物質の炭素被覆量が、前記電極活物質の質量に対して0.5質量%以上3.0質量%以下であり、
 前記フッ化ビニリデン共重合体の重量平均分子量Mwaが50000以上であり、
 前記フッ化ビニリデン共重合体を、2-ブロモメチルピレンからなる標識物質で修飾し、波長345nmの光を吸収するカルボキシ基含有フッ化ビニリデン共重合体の重量平均分子量Mwcを特定したとき、
 前記Mwcが、前記Mwaに対して、0.90未満である、
 電極合剤。
a vinylidene fluoride copolymer having a structural unit derived from vinylidene fluoride and a structural unit derived from a vinyl compound having a carboxy group;
a carbon-coated electrode active material;
An electrode mixture comprising:
The amount of carbon coating on the electrode active material is 0.5% by mass or more and 3.0% by mass or less with respect to the mass of the electrode active material,
The weight average molecular weight M of the vinylidene fluoride copolymer is 50,000 or more,
When the vinylidene fluoride copolymer is modified with a labeling substance consisting of 2-bromomethylpyrene and the weight average molecular weight Mwc of the carboxy group-containing vinylidene fluoride copolymer that absorbs light at a wavelength of 345 nm is specified,
The Mwc is less than 0.90 relative to the Mwa.
Electrode mixture.
 前記Mwcが、前記Mwaに対して、0.25以上である、
 請求項1に記載の電極合剤。
The Mwc is 0.25 or more relative to the Mwa.
The electrode mixture according to claim 1 .
 前記電極活物質の平均粒子径が15μm以下である、
 請求項1に記載の電極合剤。
The average particle size of the electrode active material is 15 μm or less.
The electrode mixture according to claim 1 .
 前記電極活物質は、前記炭素被覆量が2.5質量%以下である、
 請求項1に記載の電極合剤。
The electrode active material has a carbon coating amount of 2.5 mass% or less.
The electrode mixture according to claim 1 .
 前記ビニル化合物が、下記一般式(1)で表される化合物である、
 請求項1に記載の電極合剤。
(一般式(1)において、
 R、R、Rはそれぞれ独立に、水素原子、ハロゲン原子、または炭素数1以上5以下のアルキル基を表し、
 Xは、ヒドロキシ基、または-Y-COOHを表す(Yは原子団を表す))
The vinyl compound is a compound represented by the following general formula (1):
The electrode mixture according to claim 1 .
(In general formula (1),
R 1 , R 2 , and R 3 each independently represent a hydrogen atom, a halogen atom, or an alkyl group having 1 to 5 carbon atoms;
X represents a hydroxy group or -Y-COOH (wherein Y represents an atomic group).
 前記ビニル化合物が、下記一般式(1)で表される化合物である、
 請求項1に記載の電極合剤。
(一般式(1)において、
 R、R、Rはそれぞれ独立に、水素原子、ハロゲン原子、または炭素数1以上5以下のアルキル基を表し、
 Xは、ヒドロキシ基、または-Y-COOHを表す(Yは酸素原子または窒素原子のいずれか一方を含み、かつ主鎖の原子数が1以上10以下である、分子量500以下の2価の原子団を表す))
The vinyl compound is a compound represented by the following general formula (1):
The electrode mixture according to claim 1 .
(In general formula (1),
R 1 , R 2 , and R 3 each independently represent a hydrogen atom, a halogen atom, or an alkyl group having 1 to 5 carbon atoms;
X represents a hydroxy group or -Y-COOH (Y represents a divalent atomic group containing either an oxygen atom or a nitrogen atom, having 1 to 10 atoms in the main chain, and having a molecular weight of 500 or less)
 請求項1~6のいずれか一項に記載の電極合剤の固形分を含む、電極。 An electrode containing the solid content of the electrode mixture described in any one of claims 1 to 6.  請求項7に記載の電極を含む、電池。
 
A battery comprising the electrode of claim 7.
PCT/JP2025/011997 2024-03-29 2025-03-26 Electrode mixture, electrode, and battery Pending WO2025205922A1 (en)

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09320607A (en) * 1996-05-27 1997-12-12 Kureha Chem Ind Co Ltd Binder for electrode formation, electrode mix and electrode structure for non-aqueous battery and the battery
JPH10233206A (en) * 1997-02-17 1998-09-02 Asahi Chem Ind Co Ltd Nonaqueous electrolyte secondary battery
WO2017056974A1 (en) * 2015-09-30 2017-04-06 株式会社クレハ Binder composition, non-aqueous electrolyte secondary battery electrode, and non-aqueous electrolyte secondary battery
WO2018008263A1 (en) * 2016-07-06 2018-01-11 株式会社クレハ Binder composition, electrode mixture, electrode, and non-aqueous electrolyte secondary battery
WO2018008262A1 (en) * 2016-07-06 2018-01-11 株式会社クレハ Binder composition, electrode mixture, electrode, non-aqueous electrolyte secondary battery, and binder composition production method

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09320607A (en) * 1996-05-27 1997-12-12 Kureha Chem Ind Co Ltd Binder for electrode formation, electrode mix and electrode structure for non-aqueous battery and the battery
JPH10233206A (en) * 1997-02-17 1998-09-02 Asahi Chem Ind Co Ltd Nonaqueous electrolyte secondary battery
WO2017056974A1 (en) * 2015-09-30 2017-04-06 株式会社クレハ Binder composition, non-aqueous electrolyte secondary battery electrode, and non-aqueous electrolyte secondary battery
WO2018008263A1 (en) * 2016-07-06 2018-01-11 株式会社クレハ Binder composition, electrode mixture, electrode, and non-aqueous electrolyte secondary battery
WO2018008262A1 (en) * 2016-07-06 2018-01-11 株式会社クレハ Binder composition, electrode mixture, electrode, non-aqueous electrolyte secondary battery, and binder composition production method

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