WO2021065742A1 - 非水系二次電池用バインダー組成物及びその製造方法、非水系二次電池電極用スラリー組成物、非水系二次電池用電極、並びに非水系二次電池 - Google Patents
非水系二次電池用バインダー組成物及びその製造方法、非水系二次電池電極用スラリー組成物、非水系二次電池用電極、並びに非水系二次電池 Download PDFInfo
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
- H01M4/621—Binders
- H01M4/622—Binders being polymers
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L53/00—Compositions of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers
- C08L53/02—Compositions of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers of vinyl-aromatic monomers and conjugated dienes
- C08L53/025—Compositions of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers of vinyl-aromatic monomers and conjugated dienes modified
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F297/00—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer
- C08F297/02—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer using a catalyst of the anionic type
- C08F297/023—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer using a catalyst of the anionic type using a coupling agent
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F8/00—Chemical modification by after-treatment
- C08F8/46—Reaction with unsaturated dicarboxylic acids or anhydrides thereof, e.g. maleinisation
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/005—Processes for mixing polymers
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L53/00—Compositions of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers
- C08L53/02—Compositions of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers of vinyl-aromatic monomers and conjugated dienes
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/052—Li-accumulators
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/052—Li-accumulators
- H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/04—Processes of manufacture in general
- H01M4/0402—Methods of deposition of the material
- H01M4/0404—Methods of deposition of the material by coating on electrode collectors
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
- H01M4/139—Processes of manufacture
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2353/00—Characterised by the use of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Derivatives of such polymers
- C08J2353/02—Characterised by the use of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Derivatives of such polymers of vinyl aromatic monomers and conjugated dienes
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2419/00—Characterised by the use of rubbers not provided for in groups C08J2407/00 - C08J2417/00
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Definitions
- the present invention relates to a binder composition for a non-aqueous secondary battery and a method for producing the same, a slurry composition for a non-aqueous secondary battery electrode, an electrode for a non-aqueous secondary battery, and a non-aqueous secondary battery.
- Non-aqueous secondary batteries such as lithium-ion secondary batteries (hereinafter, may be simply abbreviated as "secondary batteries") are small and lightweight, have high energy density, and can be repeatedly charged and discharged. Yes, it is used for a wide range of purposes. Therefore, in recent years, improvement of battery members such as electrodes has been studied for the purpose of further improving the performance of non-aqueous secondary batteries.
- the electrodes used in a secondary battery such as a lithium ion secondary battery are usually a current collector and an electrode mixture layer (positive electrode mixture layer or negative electrode mixture layer) formed on the current collector. It has. Then, in this electrode mixture layer, for example, a slurry composition containing an electrode active material and a binder composition containing a binder is applied onto a current collector, and the applied slurry composition is dried. It is formed.
- polymer particles containing a polymer having a block region composed of a predetermined monomer unit have been conventionally used.
- Patent Document 1 an aqueous dispersion of polymer particles containing a block polymer containing a methacrylic acid unit in a graft portion is used by using a cyclohexane solution of a block polymer in which a graft portion in which methacrylic acid units are connected is introduced.
- the present invention discloses a binder composition for a non-aqueous secondary battery, which comprises such an aqueous dispersion, a water-soluble polymer having a hydrophilic group and a weight average molecular weight within a predetermined range, and water. ..
- the adhesion between the electrode mixture layer and the current collector is enhanced, that is, the peel strength of the electrode is enhanced, and the electrode is used. It is required to enhance the viscosity stability of the slurry composition used when forming the mixture layer.
- the electrode formed by using the above-mentioned conventional binder composition has room for further improvement in peel strength.
- the present invention provides a slurry composition for a non-aqueous secondary battery electrode having excellent viscosity stability and a binder composition for a non-aqueous secondary battery capable of forming an electrode for a non-aqueous secondary battery having excellent peel strength.
- the purpose is to do.
- Another object of the present invention is to provide a slurry composition for a non-aqueous secondary battery electrode capable of forming an electrode for a non-aqueous secondary battery having excellent peel strength and having excellent viscosity stability.
- a further object of the present invention is to provide an electrode for a non-aqueous secondary battery having excellent peel strength and a non-aqueous secondary battery including the electrode for the non-aqueous secondary battery.
- the present inventor conducted a diligent study for the purpose of solving the above problems. Then, the present inventor has conceived to include polymer particles containing two kinds of polymers having different properties in the binder composition. Further, in the binder composition, one of the polymers contained in the polymer particles is a block polymer having an acidic group-containing monomer unit, and the other is an acidic group-containing monomer unit.
- a slurry composition for a non-aqueous secondary battery electrode having excellent viscosity stability when the polymer does not have and the total content ratio of the aliphatic conjugated diene monomer unit and the alkylene structural unit is a predetermined value or more.
- the present invention has been completed by finding that it is possible to form an electrode for a non-aqueous secondary battery having excellent peel strength.
- the present invention aims to advantageously solve the above problems, and the binder composition for a non-aqueous secondary battery of the present invention is a binder composition for a non-aqueous secondary battery containing polymer particles.
- the polymer particles include a polymer 1 which is a block polymer having an acidic group-containing monomer unit and a polymer 2 which does not have an acidic group-containing monomer unit. Based on the total mass of 1 and the polymer 2, the proportion of the polymer 1 is 10% by mass or more and 90% by mass or less, and the polymer 2 is an aliphatic conjugated diene monomer unit and an alkylene structural unit.
- the total ratio of the aliphatic conjugated diene monomer unit and the alkylene structural unit is 55% by mass or more, based on the total mass of all the repeating units contained in the polymer 2. , Characterized by. As described above, if a binder composition containing polymer particles containing the above-mentioned predetermined polymer 1 and polymer 2 in a predetermined ratio is used, it is suitable for a non-aqueous secondary battery electrode having excellent viscosity stability. It is possible to form a slurry composition and an electrode for a non-aqueous secondary battery having excellent peel strength.
- the "monomer unit" of the polymer means "a repeating unit derived from the monomer contained in the polymer obtained by using the monomer".
- the "content ratio (mass%)" of each repeating unit in the polymer can be measured by using a nuclear magnetic resonance (NMR) method such as 1 H-NMR. Further, the ratio of the polymer 1 based on the total mass of the polymer 1 and the polymer 2 can be measured by a method of separation and quantification using the difference in electric charge such as normal phase chromatography.
- NMR nuclear magnetic resonance
- the polymer 1 has a main chain containing a block region composed of an aromatic vinyl monomer unit and a graft portion bonded to the main chain.
- the proportion of the aromatic vinyl monomer unit is 10% by mass or more and 50% by mass or less based on the total mass of all the repeating units contained in the main chain, and the graft portion is covered with the above. It preferably contains an acidic group-containing monomer unit.
- the ratio of the aromatic vinyl monomer unit in the main chain of the polymer 1 is 10% by mass or more and 50% by mass or less, the peel strength of the electrode formed by using the binder composition can be improved.
- the internal resistance of the obtained secondary battery can be reduced. Further, if the acidic group-containing monomer unit is contained in the graft portion, the viscosity stability of the obtained slurry composition can be further enhanced.
- “including a block region composed of a monomer unit” means that "a portion in a polymer in which only the monomer unit is connected in a row exists as a repeating unit”.
- the acid value of the polymer 1 is preferably 0.5 mgCH 3 ONa / g or more and 30 mgCH 3 ONa / g or less.
- the acid value of the polymer 1 is within the above-mentioned predetermined range, the viscosity stability of the slurry composition obtained by using the binder composition and the peel strength of the obtained electrode can be further improved. , The internal resistance of the obtained secondary battery can be reduced.
- the acid value of the polymer 1 can be measured by the method described in Examples.
- the polymer 2 is a block polymer. If the polymer particles contained in the binder composition contain a predetermined block polymer as the polymer 2, the peel strength of the obtained electrode can be further improved.
- the polymer 1 contains at least one of an aliphatic conjugated diene monomer unit and an alkylene structural unit. If the polymer 1 contains at least one of an aliphatic conjugated diene monomer unit and an alkylene structural unit, the flexibility of the obtained electrode mixture layer can be increased, and a secondary having such an electrode mixture layer is provided. The internal resistance of the battery can be further reduced.
- the acidic group-containing monomer unit of the polymer 1 is a carboxyl group-containing monomer unit. If the polymer 1 has a carboxyl group-containing monomer unit, the viscosity stability of the obtained slurry composition can be further enhanced, and the peel strength of the obtained electrode can be further enhanced.
- the present invention aims to advantageously solve the above problems, and the method for producing a binder composition for a non-aqueous secondary battery of the present invention comprises the polymer 1, the polymer 2, and an organic substance. It is characterized by including a step of obtaining a premix containing a solvent, an emulsifier, and water, and a phase inversion emulsification step of inversion emulsifying the premix. As described above, by obtaining a predetermined premix and then inversion emulsifying the premix, any of the above-mentioned binder compositions for non-aqueous secondary batteries of the present invention can be easily produced.
- the present invention also aims to advantageously solve the above problems, and the slurry composition for a non-aqueous secondary battery electrode of the present invention comprises an electrode active material and any of the above-mentioned non-aqueous secondary batteries. It is characterized by containing a binder composition for a secondary battery.
- the slurry composition for a non-aqueous secondary battery electrode containing the electrode active material and any of the above-mentioned binder compositions for a non-aqueous secondary battery has excellent viscosity stability and peel strength. It is possible to form an excellent electrode.
- the present invention aims to advantageously solve the above problems, and the electrode for a non-aqueous secondary battery of the present invention is formed by using the above-mentioned slurry composition for a non-aqueous secondary battery electrode. It is characterized by providing a formed electrode mixture layer. As described above, the electrode for a non-aqueous secondary battery provided with the electrode mixture layer formed by using the above-mentioned slurry composition for the non-aqueous secondary battery electrode is excellent in peel strength.
- the present invention aims to solve the above problems advantageously, and the non-aqueous secondary battery of the present invention is characterized by including the above-mentioned electrode for the non-aqueous secondary battery.
- the electrode for a non-aqueous secondary battery described above a non-aqueous secondary battery capable of exhibiting excellent performance such as high output characteristics can be obtained.
- a slurry composition for a non-aqueous secondary battery electrode having excellent viscosity stability and a binder composition for a non-aqueous secondary battery capable of forming an electrode for a non-aqueous secondary battery having excellent peel strength. can do.
- the binder composition for a non-aqueous secondary battery of the present invention is used for manufacturing a non-aqueous secondary battery, and is particularly preferably used for manufacturing an electrode of a non-aqueous secondary battery. it can.
- the binder composition for a non-aqueous secondary battery of the present invention can be used for preparing the slurry composition for a non-aqueous secondary battery electrode of the present invention.
- the slurry composition prepared by using the binder composition of the present invention can be used when producing an electrode of a non-aqueous secondary battery such as a lithium ion secondary battery.
- the non-aqueous secondary battery of the present invention is characterized by using the electrode for the non-aqueous secondary battery of the present invention formed by using the slurry composition of the present invention.
- the binder composition for a non-aqueous secondary battery, the slurry composition for a non-aqueous secondary battery electrode, and the electrode for a non-aqueous secondary battery of the present invention are preferably for a negative electrode, and the non-aqueous secondary battery of the present invention is used.
- the battery preferably uses the electrode for a non-aqueous secondary battery of the present invention as a negative electrode.
- the binder composition of the present invention contains predetermined polymer particles, and may optionally further contain a solvent such as water and other components that can be incorporated into the binder composition.
- the polymer particles are a block polymer having an acidic group-containing monomer unit, a polymer 1, and a polymer 2 having no acidic group-containing monomer unit.
- the ratio of the polymer 1 is 10% by mass or more and 90% by mass or less based on the total mass of the polymer 1 and the polymer 2, and the polymer 2 is an aliphatic conjugated diene monomer unit and When the total ratio of the aliphatic conjugated diene monomer unit and the alkylene structural unit, which contains at least one of the alkylene structural units and is based on the total mass of all the repeating units contained in the polymer 2, is 55% by mass or more. It is characterized by being.
- binder composition of the present invention a slurry composition for a non-aqueous secondary battery electrode having excellent viscosity stability and a non-aqueous secondary battery capable of forming an electrode for a non-aqueous secondary battery having excellent peel strength can be formed.
- Binder compositions for batteries can be provided.
- the polymer particles By making the polymer particles have the above composition, it is possible to prepare a slurry composition for a non-aqueous secondary battery electrode having excellent viscosity stability, and for a non-aqueous secondary battery having excellent peel strength.
- the reason why the electrode can be formed is not clear, but it is presumed to be as follows. That is, the polymer 1 containing the acidic group-containing monomer unit acts to increase the viscosity stability of the slurry composition mainly by increasing the dispersion stability of the polymer particles in a solvent such as water. It is considered that this is because the polymer 2 acts to impart flexibility to the polymer particles, and due to these synergistic effects, it functions to increase the peel strength of the electrode from which the polymer particles are obtained.
- the polymer particles are components that function as a binder, and when an electrode mixture layer is formed using a slurry composition containing a binder composition, components such as an electrode active material are released from the electrode mixture layer. It is a component that can hold the electrode mixture layer so as not to be detached, bring the electrode mixture layer into close contact with the current collector, and enable adhesion between the electrode and the separator via the electrode mixture layer.
- the polymer particles are water-insoluble particles containing at least the polymer 1 and the polymer 2.
- the polymer particles contain at least the polymer 1 and the polymer 2, and are components other than the polymer 1 and the polymer 2, such as a component that is inevitably mixed in the preparation stage of various polymers and the preparation stage of the polymer particles. May include.
- water-insoluble means that when 0.5 g of particles are dissolved in 100 g of water at a temperature of 25 ° C., the insoluble content is 90% by mass or more.
- the polymer 1 contained in the polymer particles is a block polymer having an acidic group-containing monomer unit. Further, the polymer 1 is bonded to a main chain containing a block region composed of aromatic vinyl monomer units (hereinafter, may be abbreviated as “aromatic vinyl block region 1”) and the main chain. It is a polymer having a grafted portion, and the proportion of aromatic vinyl monomer units is 10% by mass or more and 50% by mass or less based on the total mass of all repeating units contained in the main chain, and the graft is used. It is preferably a polymer containing an acidic group-containing monomer unit in a portion.
- the peel strength of the electrode formed by using the binder composition can be improved.
- the internal resistance of the obtained secondary battery can be reduced.
- the acidic group-containing monomer unit is contained in the graft portion of the polymer 1, the viscosity stability of the obtained slurry composition can be further enhanced.
- the polymer 1 is abbreviated as a polymer chain portion (hereinafter, abbreviated as "other region") in which a repeating unit other than the aromatic vinyl monomer unit is connected in addition to the aromatic vinyl block region 1.
- it is preferable that it is a copolymer having ().
- the aromatic vinyl block region and the other regions are adjacent to each other.
- the polymer 1 may have only one aromatic vinyl block region, may have a plurality of aromatic vinyl block regions, and may have only one other region, and may have a plurality of other regions. You may be doing it.
- the aromatic vinyl block region 1 is a region containing only the aromatic vinyl monomer unit as the repeating unit.
- one aromatic vinyl block region 1 may be composed of only one kind of aromatic vinyl monomer unit, or may be composed of a plurality of kinds of aromatic vinyl monomer units. However, it is preferable that it is composed of only one kind of aromatic vinyl monomer unit.
- one aromatic vinyl block region 1 may include a coupling portion (that is, the aromatic vinyl monomer unit constituting one aromatic vinyl block region is interposed with a coupling portion. It may be connected).
- the types and proportions of the aromatic vinyl monomer units constituting the plurality of aromatic vinyl block regions 1 may be the same or different. However, it is preferable that they are the same.
- Examples of the aromatic vinyl monomer capable of forming the aromatic vinyl monomer unit constituting the aromatic vinyl block region 1 of the polymer 1 include styrene, ⁇ -methylstyrene, pt-butylstyrene, and butoxy. Examples thereof include styrene, vinyltoluene, chlorostyrene, and vinylnaphthalene. Of these, styrene is preferable. These can be used individually by 1 type or in combination of 2 or more types, but it is preferable to use 1 type alone.
- the ratio of the aromatic vinyl monomer unit in the polymer 1 is 10% by mass or more based on the total mass of all the repeating units contained in the main chain of the polymer 1 (100% by mass). It is preferably 15% by mass or more, more preferably 50% by mass or less, and even more preferably 45% by mass or less.
- the ratio of the aromatic vinyl monomer unit is equal to or higher than the above lower limit value, it is possible to suppress the strength of the polymer particles from becoming excessively low, and the electrode mixture layer when the electrode mixture layer is formed can be used. Adhesion with the current collector can be improved. As a result, the peel strength of the obtained electrode can be further increased.
- the ratio of the aromatic vinyl monomer unit in the main chain of the polymer 1 is usually the same as the ratio of the aromatic vinyl block region 1 in the main chain of the polymer 1.
- the other region is a region containing only a repeating unit other than the aromatic vinyl monomer unit (hereinafter, may be abbreviated as “other repeating unit”) as the repeating unit.
- one other region may be composed of one kind of other repeating unit, or may be composed of a plurality of kinds of other repeating units.
- one other region may include a coupling site (that is, the other repeating units constituting one other region may be connected with the coupling site interposed therebetween). ..
- the types and proportions of the other repeating units constituting the plurality of other regions may be the same or different.
- the other repeating unit constituting the other region of the polymer 1 is not particularly limited, and is, for example, an aliphatic conjugated diene monomer unit, an alkylene structural unit, and an ⁇ , ⁇ -unsaturated nitrile monomer unit. Can be mentioned. Above all, the polymer 1 preferably contains at least one of an aliphatic conjugated diene monomer unit and an alkylene structural unit.
- examples of the aliphatic conjugated diene monomer capable of forming the aliphatic conjugated diene monomer unit constituting the other region include 1,3-butadiene and 2-methyl-1,3-butadiene (isoprene). ), 2,3-dimethyl-1,3-butadiene, 2-chlor-1,3-butadiene; pentadiene having a conjugated double bond in the main chain and its substitution product; and having a conjugated double bond in the side chain. Hexadiene and its substitutes; and the like. These can be used alone or in combination of two or more.
- the alkylene structural units constituting the other areas have the general formula: -C n H 2n - [where, n is an integer of 2 or more is a repeating unit composed of only alkylene structure represented by.
- the alkylene structural unit may have, for example, 8 or less carbon atoms, preferably 6 or less carbon atoms.
- the alkylene structural unit may be linear or branched.
- the method for introducing the alkylene structural unit into the polymer 1 is not particularly limited.
- the aliphatic conjugated diene monomer unit is converted into an alkylene structural unit and is heavy.
- the polymer 1 can be produced by the method of obtaining the coalescence 1.
- the selective hydrogenation of the aliphatic conjugated diene monomer unit can be carried out by using a known method such as an oil layer hydrogenation method or an aqueous layer hydrogenation method.
- the polymer 1 contains at least one of the aliphatic conjugated diene monomer unit and the alkylene structural unit
- the total mass of the aliphatic conjugated diene monomer unit and the alkylene structural unit in the polymer 1 The ratio is preferably 50% by mass or more, more preferably 55% by mass or more, and 90% by mass, based on the total mass of all repeating units contained in the main chain of the polymer 1 (100% by mass). % Or less, more preferably 85% by mass or less.
- the peel strength of the obtained electrode can be further enhanced by increasing the flexibility of the polymer particles. it can.
- the peel strength of the obtained electrode is further increased by further increasing the strength of the polymer particles. be able to.
- the polymer 1 preferably contains a graft portion. More specifically, it is preferable that the polymer 1 contains a graft moiety containing an acidic group-containing monomer unit as a repeating unit.
- the bonding position of the graft portion with respect to the main chain of the polymer 1 is not particularly limited, but the polymer 1 is at least one of [aromatic vinyl block region 1] and [aliphatic conjugated diene monomer unit and alkylene structural unit]. If it contains [other regions], the graft moiety can be attached to [other regions].
- the frequency of the acidic group-containing monomer unit in the vicinity of the surface layer of the polymer particles is higher than that inside the polymer particles. This makes it possible to improve the particle stability and dispersion stability of the polymer particles in a solvent such as water.
- Examples of the acidic group-containing monomer capable of forming an acidic group-containing monomer unit include a carboxyl group-containing monomer, a sulfonic acid group-containing monomer, and a phosphoric acid group-containing monomer.
- the acidic group-containing monomer capable of forming the acidic group-containing monomer unit does not include those corresponding to the aromatic vinyl monomer and the aliphatic conjugated diene monomer.
- Examples of the carboxyl group-containing monomer include monocarboxylic acid and its derivative, dicarboxylic acid and its acid anhydride, and their derivatives.
- Examples of the monocarboxylic acid include acrylic acid, methacrylic acid, and crotonic acid.
- Examples of the monocarboxylic acid derivative include 2-ethylacrylic acid, isocrotonic acid, ⁇ -acetoxyacrylic acid, ⁇ -trans-aryloxyacrylic acid, ⁇ -chloro- ⁇ -E-methoxyacrylic acid and the like.
- Examples of the dicarboxylic acid include maleic acid, fumaric acid, and itaconic acid.
- Dicarboxylic acid derivatives include methylmaleic acid, dimethylmaleic acid, phenylmaleic acid, chloromaleic acid, dichloromaleic acid, fluoromaleic acid, nonyl maleate, decyl maleate, dodecyl maleate, octadecyl maleate, fluoromaleate.
- Maleic acid monoesters such as alkyl can be mentioned.
- Examples of the acid anhydride of the dicarboxylic acid include maleic anhydride, acrylic anhydride, methyl maleic anhydride, and dimethyl maleic anhydride.
- an acid anhydride that produces a carboxyl group by hydrolysis can also be used.
- sulfonic acid group-containing monomer examples include styrene sulfonic acid, vinyl sulfonic acid (ethylene sulfonic acid), methyl vinyl sulfonic acid, (meth) allyl sulfonic acid, and 3-allyloxy-2-hydroxypropane sulfonic acid.
- styrene sulfonic acid vinyl sulfonic acid (ethylene sulfonic acid), methyl vinyl sulfonic acid, (meth) allyl sulfonic acid, and 3-allyloxy-2-hydroxypropane sulfonic acid.
- (meth) allyl means allyl and / or allyl.
- examples of the phosphate group-containing monomer include -2- (meth) acryloyloxyethyl phosphate, methyl-2- (meth) acryloyloxyethyl phosphate, and ethyl phosphate- (meth) acryloyloxyethyl.
- (meth) acryloyl means acryloyl and / or methacryloyl.
- one type of the above-mentioned monomer forming the repeating unit contained in the graft portion of the polymer 1 may be used alone, or two or more types may be used in combination.
- the monomer forming the repeating unit contained in the graft portion of the polymer 1 the above-mentioned carboxyl group-containing monomer is preferable, and among them, the self-polymerizability is low and it becomes an impurity of the binder composition.
- Maleic acid and maleic anhydride are preferred because they are less likely to produce a capable polymer or oligomer.
- the method of introducing the graft portion into the polymer 1 is not particularly limited.
- a polymer having an aromatic vinyl block region and another region containing an aliphatic conjugated diene monomer unit is prepared, and the polymer is used as a trunk portion (main chain), and the above-mentioned acidic group-containing single amount is used.
- a radical initiator such as a redox initiator
- a polymer 1 having a structure in which the polymer of the graft portion is bonded to the main chain of the polymer can be obtained. it can.
- Polymer 1 had an acid value is preferably at 0.5mgCH 3 ONa / g or more, more preferably 2.0mgCH 3 ONa / g or more, not less 5.0mgCH 3 ONa / g or more more preferably, it is preferably less 30mgCH 3 ONa / g, more preferably 20mgCH 3 ONa / g or less, and more preferably less 12mgCH 3 ONa / g.
- the acid value of the polymer 1 is at least the above lower limit value, the stability of the polymer particles can be enhanced, and the viscosity stability of the obtained slurry composition can be further enhanced.
- the peel strength of the obtained electrode can be increased.
- the flexibility of the polymer particles can be increased.
- the acid value of the polymer is not more than the above upper limit value, the internal resistance of the obtained secondary battery can be further reduced.
- the acid value value of the polymer 1 indicates the amount of the acidic group-containing monomer unit contained in the polymer 1.
- the amount of the acidic group-containing monomer and the polymerization initiator added at the time of graft polymerization, the polymerization time and the like are appropriately adjusted to obtain the polymer 1 having a desired acid value. be able to.
- the polymer 1 is polymerized, for example, by adding a second monomer component different from the first monomer component to a solution obtained by polymerizing the first monomer component in an organic solvent. If necessary, it can be prepared by further repeating the addition of the monomer component and the polymerization.
- the organic solvent used as the reaction solvent is not particularly limited, and can be appropriately selected depending on the type of the monomer and the like. In preparing the polymer 1 which is a block polymer, it may be subjected to a coupling reaction using a coupling agent.
- the ends of the diblock structures contained in the block polymer can be bound to each other with a coupling agent to be converted into a triblock structure.
- the coupling agent that can be used in the coupling reaction is not particularly limited, and examples thereof include known bifunctional or higher functional coupling agents.
- the polymer 1 can be synthesized according to the above-mentioned method, but can also be obtained as a commercially available product. Furthermore, the polymer 1 can also be obtained by graft-polymerizing an acidic group-containing monomer with a commercially available polymer that does not contain a commercially available acidic group-containing monomer unit.
- Examples of products that can be used as the polymer 1 include Tough Tech (registered trademark) M series (manufactured by Asahi Kasei Co., Ltd., maleic anhydride-modified SEBS (styrene-ethylene / butylene-styrene)) and Kraton (registered trademark) FG series. (Manufactured by Kraton Polymer Co., Ltd., maleic anhydride-modified SEBS) and the like.
- the polymer 2 contained in the polymer particles does not contain an acidic group-containing monomer unit.
- the acidic group-containing monomer unit is as described above for the polymer 1, and the polymer 2 is characterized by not containing such an acidic group-containing monomer unit.
- the polymer 2 contains at least one of an aliphatic conjugated diene monomer unit and an alkylene structural unit, and the total mass of all the repeating units contained in the polymer 2 is used as a reference (100% by mass).
- the total ratio of the aliphatic conjugated diene monomer unit and the alkylene structural unit is 55% by mass or more, which is a polymer.
- the polymer particles may contain not only one type but also a plurality of types of components corresponding to the polymer 2.
- the polymer 2 can be a random polymer or a block polymer without particular limitation, but among them, a block polymer is preferable. If the polymer particles contain a predetermined block polymer as the polymer 2, the peel strength of the obtained electrode can be further improved.
- the aliphatic conjugated diene monomer unit and the alkylene structural unit that can be contained in the polymer 2 are the same units as the aliphatic conjugated diene monomer unit and the alkylene structural unit that the polymer 1 can contain as other repeating units. Can be mentioned.
- the polymer 2 contains an aliphatic conjugated diene monomer unit.
- the aliphatic conjugated diene monomer unit of the polymer 2 preferably contains 1,3-butadiene monomer unit or isoprene monomer unit, and from the viewpoint of further enhancing the peel strength of the obtained electrode, 1 , 3-butadiene monomer unit is more preferable.
- the total ratio of the aliphatic conjugated diene monomer unit and the alkylene structural unit in the polymer 2 is 55% by mass or more based on the total mass of all the repeating units contained in the polymer 2 (100% by mass). It is necessary to have a certain amount, preferably 60% by mass or more, and preferably 95% by mass or less.
- the total ratio of the aliphatic conjugated diene monomer unit and the alkylene structural unit in the polymer 2 is 100%, that is, the polymer 2 is a polymer composed of only the aliphatic conjugated diene monomer unit and the alkylene structural unit. You may.
- the flexibility of the polymer particles can be increased, and as a result, the internal resistance of the obtained secondary battery can be further reduced. Further, when the total ratio in the polymer 2 is not more than the above upper limit value, the strength of the polymer particles can be further increased, and as a result, the peel strength of the obtained electrode can be increased.
- the polymer 2 may optionally have other units other than the above. Examples of such a unit include an aromatic vinyl monomer unit and an ⁇ , ⁇ -unsaturated nitrile monomer unit as described above for the polymer 1.
- the polymer 2 is more than the aromatic vinyl monomer unit in addition to the block region containing at least one of the aliphatic conjugated diene monomer unit and the alkylene structural unit. It is preferable to have a block region (hereinafter, may be abbreviated as “aromatic vinyl block region 2”).
- the aromatic vinyl block region 2 is the same as the content described in detail for the aromatic vinyl block region 1 of the polymer 1. If the polymer 2 contains the aromatic vinyl block region 2, the peel strength of the obtained electrode can be further increased.
- the ratio of other units in the polymer 2 is preferably 5% by mass or more and 45% by mass or less, based on the total mass of all repeating units contained in the polymer 2 (100% by mass). ..
- the proportion of the polymer 1 needs to be 10% by mass or more based on the total mass of the above-mentioned polymer 1 and the polymer 2 (100% by mass). It is preferably 20% by mass or more, more preferably 30% by mass or more, needs to be 90% by mass or less, more preferably 80% by mass or less, and more preferably 70% by mass or less. More preferred.
- the ratio of the polymer 1 is at least the above lower limit value, the stability of the polymer particles in the slurry composition can be enhanced, and the viscosity stability of the slurry composition can be enhanced. Further, when the ratio of the polymer 1 is not more than the above upper limit value, the peel strength of the obtained electrode can be increased.
- the polymer particles may contain known additives.
- known additives include antioxidants and the like.
- the antioxidant is not particularly limited, and is, for example, 4-[[4,6-bis (octylthio) -1,3,5-triazine-2-yl] amino] -2,6-di. -Hinderdphenolic antioxidants such as tert-butylphenol; phosphites such as 3,9-bis (octadecyloxy) -2,4,8,10-tetraoxa-3,9-diphosphaspiro [5.5] undecane Antioxidants; etc.
- the method for preparing the polymer particles containing the polymer 1 and the polymer 2 described above is not particularly limited.
- the above-mentioned predetermined polymer particles have a step of obtaining a premix containing polymer 1, polymer 2, an organic solvent, an emulsifier, and water (premix step) and a step of inversion emulsifying the obtained premix. It can be easily prepared through a phase emulsification step.
- a premix containing polymer 1, polymer 2, an organic solvent, an emulsifier, and water is obtained.
- the procedure for obtaining such a premixture is not particularly limited.
- a premixture can be obtained by dissolving both the polymer 1 and the polymer 2 in an organic solvent and then mixing them with an emulsifier and water.
- the polymerization reaction solution can be used as it is as the polymer solution. ..
- organic solvent a known organic solvent such as cyclohexane can be appropriately selected and used according to the composition of the polymer 1 and the polymer 2.
- emulsifier a known emulsifier such as sodium alkylbenzene sulfonate can be appropriately selected and used depending on the properties of the organic solvent used, the composition of the polymer 1 and the polymer 2, and the like.
- phase inversion emulsification in the phase inversion emulsification step is not particularly limited, and for example, the premix obtained in the above-mentioned premixing step can be phase inversion emulsified using an emulsification disperser.
- the emulsification disperser is not particularly limited, and for example, the product name "homogenizer” (manufactured by IKA), the product name "Polytron” (manufactured by Kinematica), and the product name "TK autohomo mixer”.
- Batch type emulsification disperser (manufactured by Special Machinery Co., Ltd.); Product name "TK Pipeline Homo Mixer” (manufactured by Special Machinery Co., Ltd.), Product name “Coloid Mill” (manufactured by Shinko Pantech Co., Ltd.), Product name “Slasher” (manufactured by Nippon Coke Industries Co., Ltd.), product name “Trigonal Wet Emulsifier” (manufactured by Mitsui Miike Kakoki Co., Ltd.), product name “Cavitron” (manufactured by Eurotech Co., Ltd.), product name “Milder” (manufactured by Pacific Kiko Co., Ltd.) , Product name “Fine Flow Mill” (manufactured by Pacific Kiko Co., Ltd.), etc.
- Continuous emulsification disperser Product name "Microfluidizer” (manufactured by Mizuho Kogyo Co., Ltd.), Product name “Nanomizer” (manufactured by Nanomizer Co., Ltd.), Product High-pressure emulsification / disperser such as name “APV Gaulin” (manufactured by Gaulin), "LAB1000” (manufactured by SPXFLOW); A vibrating emulsification disperser such as “Vibro Mixer” (manufactured by Cooling Industry Co., Ltd.); an ultrasonic emulsification disperser such as "Ultrasonic Homogenizer” (manufactured by Branson Co., Ltd.) can be used.
- the conditions for the emulsification operation by the emulsification disperser are not particularly limited, and may be appropriately selected so as to obtain a desired dispersion state. Then, an aqueous dispersion of polymer particles containing the polymer 1 and the polymer 2 can be obtained from the emulsion obtained after the phase inversion emulsification by, if necessary, removing an organic solvent by a known method or the like. it can.
- the binder composition of the present invention may contain components other than the above components (other components).
- the binder composition may contain known particulate binders (styrene butadiene random copolymer, acrylic polymer, etc.) other than the polymer particles described above.
- the binder composition may also contain known additives. Examples of such known additives include the additives listed above as additives that can be contained in the polymer particles, as well as defoamers, dispersants, thickeners, and the like.
- the binder composition may optionally contain water as a solvent and a small amount of an organic solvent. Such an organic solvent may be a residue of the organic solvent used in producing the polymer particles.
- one type may be used alone, or two or more types may be used in combination at an arbitrary ratio.
- the method for producing a binder composition of the present invention includes preparing polymer particles according to the above-mentioned method for preparing polymer particles. That is, the method for producing a binder composition of the present invention includes at least the above-mentioned premixing step and phase inversion emulsification step. Then, the method for producing the binder composition of the present invention optionally adds a desired additive to the aqueous dispersion of the polymer particles containing the polymer 1 and the polymer 2 obtained through the phase inversion emulsification step. Etc. may be further included.
- the slurry composition of the present invention is a composition used for forming an electrode mixture layer of an electrode, contains the above-mentioned binder composition, and further contains an electrode active material. That is, the slurry composition of the present invention contains the above-mentioned polymer particles and electrode active material, and optionally further contains water as a solvent and other components. Since the slurry composition of the present invention contains the binder composition described above, it is excellent in viscosity stability. Further, by using the slurry composition of the present invention, it is possible to form an electrode having excellent peel strength.
- the binder composition As the binder composition, the above-mentioned binder composition of the present invention is used.
- the blending amount of the binder composition in the slurry composition is not particularly limited.
- the blending amount of the binder composition can be such that the amount of the polymer particles is 0.5 parts by mass or more and 15 parts by mass or less in terms of solid content per 100 parts by mass of the electrode active material.
- the electrode active material is not particularly limited, and a known electrode active material used in a secondary battery can be used.
- the electrode active material that can be used in the electrode mixture layer of the lithium ion secondary battery as an example of the secondary battery is not particularly limited, and the following electrode active material may be used. it can.
- Examples of the positive electrode active material to be blended in the positive electrode mixture layer of the positive electrode of the lithium ion secondary battery include a compound containing a transition metal, for example, a transition metal oxide, a transition metal sulfide, and a composite of lithium and a transition metal.
- a metal oxide or the like can be used.
- Examples of the transition metal include Ti, V, Cr, Mn, Fe, Co, Ni, Cu, and Mo.
- the positive electrode active material is not particularly limited, and lithium-containing cobalt oxide (LiCoO 2 ), lithium manganate (LiMn 2 O 4 ), lithium-containing nickel oxide (LiNiO 2 ), Li [ Ni 5/10 Co 2/10 Mn 3/10 ] O 2 and other Co—Ni—Mn lithium-containing composite oxides, Ni—Mn—Al lithium-containing composite oxides, Ni—Co-Al lithium-containing composites Oxide, lithium olivine-type lithium iron phosphate (LiFePO 4 ), lithium olivine-type lithium manganese phosphate (LiMnPO 4 ), lithium excess spinel compound represented by Li 1 + x Mn 2-x O 4 (0 ⁇ X ⁇ 2), Examples thereof include Li [Ni 0.17 Li 0.2 Co 0.07 Mn 0.56 ] O 2 and LiNi 0.5 Mn 1.5 O 4.
- the above-mentioned positive electrode active material may be used alone or in combination of two or more.
- Examples of the negative electrode active material blended in the negative electrode mixture layer of the negative electrode of the lithium ion secondary battery include a carbon-based negative electrode active material, a metal-based negative electrode active material, and a negative electrode active material combining these.
- the carbon-based negative electrode active material refers to an active material having carbon as a main skeleton to which lithium can be inserted (also referred to as “dope”).
- Specific examples of the carbon-based negative electrode active material include coke, mesocarbon microbeads (MCMB), mesophase pitch-based carbon fiber, pyrolyzed vapor-grown carbon fiber, phenolic resin calcined product, and graphite-nitrile-based carbon fiber.
- the metal-based negative electrode active material is an active material containing a metal, and usually contains an element into which lithium can be inserted in the structure, and the theoretical electric capacity per unit mass when lithium is inserted is 500 mAh /.
- the metal-based active material for example, a lithium metal or a simple substance metal capable of forming a lithium alloy (for example, Ag, Al, Ba, Bi, Cu, Ga, Ge, In, Ni, P, Pb, Sb, Si) , Sn, Sr, Zn, Ti, etc.) and their oxides, sulfides, nitrides, silicides, carbides, phosphates and the like. Further, oxides such as lithium titanate can be mentioned.
- the above-mentioned negative electrode active material may be used alone or in combination of two or more.
- Other components that can be blended in the slurry composition include, without particular limitation, the same as those of the conductive material and other components that can be blended in the binder composition of the present invention.
- the other components one type may be used alone, or two or more types may be used in combination at an arbitrary ratio.
- the method for preparing the slurry composition is not particularly limited.
- the binder composition, the electrode active material, and other components used as needed can be mixed in the presence of an aqueous medium to prepare a slurry composition.
- the solvent such as water used in the preparation of the slurry composition includes those contained in the binder composition.
- the mixing method is not particularly limited, but the mixture can be mixed using a stirrer or a disperser that can be usually used.
- the electrode for a non-aqueous secondary battery of the present invention includes an electrode mixture layer formed by using the above-mentioned slurry composition for a non-aqueous secondary battery electrode. Therefore, the electrode mixture layer is made of a dried product of the above-mentioned slurry composition, and usually contains an electrode active material and a component derived from polymer particles, and optionally contains other components. Each component contained in the electrode mixture layer was contained in the above-mentioned slurry composition for a non-aqueous secondary battery electrode, and a suitable abundance ratio of each component is the slurry composition. It is the same as the preferable abundance ratio of each component in.
- the polymer particles are present in the particle shape in the slurry composition, but may be in the particle shape in the electrode mixture layer formed by using the slurry composition, or may be in any other shape. There may be.
- the electrode for a non-aqueous secondary battery of the present invention is excellent in peel strength because the electrode mixture layer is formed by using the above-mentioned slurry composition for a non-aqueous secondary battery electrode.
- the electrode mixture layer of the electrode for a non-aqueous secondary battery of the present invention can be formed by, for example, the following method. 1) A method in which the slurry composition of the present invention is applied to the surface of a current collector and then dried; 2) A method of immersing a current collector in the slurry composition of the present invention and then drying it; and 3) Applying the slurry composition of the present invention on a release substrate and drying it to produce an electrode mixture layer. Then, the method of transferring the obtained electrode mixture layer to the surface of the current collector.
- the method 1) is particularly preferable because it is easy to control the layer thickness of the electrode mixture layer.
- the method 1) is described in detail in a step of applying the slurry composition onto the current collector (coating step) and a step of drying the slurry composition applied on the current collector and performing electrodes on the current collector. Includes a step of forming a mixture layer (drying step).
- the method for applying the slurry composition onto the current collector is not particularly limited, and a known method can be used. Specifically, as the coating method, a doctor blade method, a dip method, a reverse roll method, a direct roll method, a gravure method, an extrusion method, a brush coating method and the like can be used. At this time, the slurry composition may be applied to only one side of the current collector, or may be applied to both sides. The thickness of the slurry film on the current collector after application and before drying can be appropriately set according to the thickness of the electrode mixture layer obtained by drying.
- the current collector to which the slurry composition is applied a material having electrical conductivity and electrochemical durability is used.
- a current collector for example, a current collector made of iron, copper, aluminum, nickel, stainless steel, titanium, tantalum, gold, platinum, or the like can be used.
- one kind of the said material may be used alone, or two or more kinds may be used in combination at an arbitrary ratio.
- the method for drying the slurry composition on the current collector is not particularly limited, and a known method can be used, for example, a drying method using warm air, hot air, low humidity air, a vacuum drying method, infrared rays, an electron beam, or the like. A drying method by irradiation can be used.
- the electrode mixture layer may be pressure-treated by using a mold press or a roll press.
- the pressurizing treatment By the pressurizing treatment, the adhesion between the electrode mixture layer and the current collector can be improved, and the obtained electrode mixture layer can be further increased in density.
- the electrode mixture layer contains a curable polymer, it is preferable to cure the polymer after the electrode mixture layer is formed.
- the non-aqueous secondary battery of the present invention includes a positive electrode, a negative electrode, an electrolytic solution, and a separator, and the above-mentioned electrode for a non-aqueous secondary battery is used as at least one of the positive electrode and the negative electrode. Since the non-aqueous secondary battery of the present invention is manufactured by using the above-mentioned electrode for a non-aqueous secondary battery as at least one of a positive electrode and a negative electrode, excellent battery characteristics can be exhibited. In the following, a case where the non-aqueous secondary battery is a lithium ion secondary battery will be described as an example, but the present invention is not limited to the following example.
- the electrode other than the above-described electrode for the non-aqueous secondary battery of the present invention which can be used in the non-aqueous secondary battery of the present invention, is not particularly limited and is used in the manufacture of the secondary battery.
- Known electrodes can be used.
- the electrode other than the electrode for the non-aqueous secondary battery of the present invention described above it is possible to use an electrode formed by forming an electrode mixture layer on the current collector using a known manufacturing method. it can.
- an organic electrolytic solution in which a supporting electrolyte is dissolved in an organic solvent is usually used.
- a lithium salt is used as the supporting electrolyte of the lithium ion secondary battery.
- the lithium salt include LiPF 6 , LiAsF 6 , LiBF 4 , LiSbF 6 , LiAlCl 4 , LiClO 4 , CF 3 SO 3 Li, C 4 F 9 SO 3 Li, CF 3 COOLi, (CF 3 CO) 2 NLi. , (CF 3 SO 2 ) 2 NLi, (C 2 F 5 SO 2 ) NLi and the like.
- LiPF 6 , LiClO 4 , and CF 3 SO 3 Li are preferable because they are easily soluble in a solvent and show a high degree of dissociation.
- One type of electrolyte may be used alone, or two or more types may be used in combination at an arbitrary ratio. Normally, the more the supporting electrolyte with a higher dissociation degree is used, the higher the lithium ion conductivity tends to be. Therefore, the lithium ion conductivity can be adjusted depending on the type of the supporting electrolyte.
- the organic solvent used in the electrolytic solution is not particularly limited as long as it can dissolve the supporting electrolyte, and for example, dimethyl carbonate (DMC), ethylene carbonate (EC), diethyl carbonate (DEC), propylene carbonate (PC), and the like.
- DMC dimethyl carbonate
- EC ethylene carbonate
- DEC diethyl carbonate
- PC propylene carbonate
- Carbonates such as butylene carbonate (BC), ethylmethyl carbonate (EMC), vinylene carbonate (VC); esters such as ⁇ -butyrolactone and methyl formate; ethers such as 1,2-dimethoxyethane and tetrahydrofuran; sulfolane, dimethyl Sulfur-containing compounds such as sulfoxide; and the like are preferably used. Further, a mixed solution of these solvents may be used.
- the dielectric constant is high and the stable potential region is wide.
- the lower the viscosity of the solvent used the higher the lithium ion conductivity tends to be. Therefore, the lithium ion conductivity can be adjusted depending on the type of solvent.
- the concentration of the electrolyte in the electrolytic solution can be adjusted as appropriate.
- known additives can be added to the electrolytic solution.
- the separator is not particularly limited, and for example, the separator described in Japanese Patent Application Laid-Open No. 2012-204303 can be used. Among these, the film thickness of the entire separator can be reduced, and as a result, the ratio of the electrode active material in the secondary battery can be increased and the capacity per volume can be increased.
- a microporous film made of a resin polyethylene, polypropylene, polybutene, polyvinyl chloride) is preferable.
- a positive electrode and a negative electrode are overlapped with each other via a separator, and the positive electrode and the negative electrode are placed in a battery container by winding or folding the battery according to the shape of the battery as necessary. It can be manufactured by injecting an electrolytic solution into the battery and sealing the container.
- the above-mentioned electrode for a non-aqueous secondary battery is used as at least one of a positive electrode and a negative electrode, preferably as a negative electrode.
- an overcurrent prevention element such as a fuse or a PTC element may be used.
- Expanded metal, lead plate, etc. may be provided.
- the shape of the secondary battery may be, for example, a coin type, a button type, a sheet type, a cylindrical type, a square type, a flat type, or the like.
- the present invention will be specifically described based on examples, but the present invention is not limited to these examples.
- “%” and “part” representing quantities are based on mass unless otherwise specified.
- the ratio of the monomer unit formed by polymerizing a certain monomer to the polymer is usually specified unless otherwise specified. It is consistent with the ratio (preparation ratio) of the certain monomer to all the monomers used in the polymer.
- the ratio of the plurality of types of polymers in the polymer particles obtained by phase inversion emulsification of the premix obtained by mixing a plurality of types of polymers is the mixing ratio of the plurality of types of polymers in the premix. Matches with. Then, in Examples and Comparative Examples, various properties were measured and various evaluations were carried out according to the following.
- ⁇ Composition of polymer> The polymers used in Examples and Comparative Examples were used as measurement samples. 1 The intensity of peaks derived from each of the aromatic vinyl monomer unit, the aliphatic conjugated diene monomer unit, and the acidic group-containing monomer unit contained in the measurement sample was calculated by H-NMR. Then, the ratio of the peak intensity derived from each monomer unit to the total peak intensity was defined as the ratio of each monomer unit in the polymer as the measurement sample. ⁇ Acid value of polymer 1> Polymer 1 was dried at 90 ° C. for 1 hour.
- ⁇ Viscosity stability of slurry composition The viscosity ⁇ 0 of the obtained slurry composition was measured using a B-type viscometer (manufactured by Toki Sangyo Co., Ltd., product name “TVB-10”, rotation speed: 60 rpm). Next, the slurry composition whose viscosity was measured was stirred for 24 hours using a planetary mixer (rotation speed: 60 rpm), and the viscosity ⁇ 1 of the stirred composition was measured with a B-type viscometer (rotation) similar to the above. Number: 60 rpm) was used for measurement.
- the viscosity change rate ⁇ ⁇ ( ⁇ 0- ⁇ 1) / ⁇ 0 ⁇ ⁇ 100 (%) of the slurry composition before and after stirring was calculated, and the viscosity stability of the slurry composition was evaluated according to the following criteria.
- the temperature at the time of viscosity measurement was 25 ° C. The closer the value of the absolute value
- is 0% or more and less than 10%
- is 10% or more and less than 20%
- is 20% More than 30%
- is 30% or more
- ⁇ Peel strength of electrodes> The prepared negative electrode was cut into a rectangle having a length of 100 mm and a width of 10 mm to obtain a test piece. This test piece was attached with cellophane tape on the surface of the negative electrode mixture layer with the surface of the negative electrode mixture layer facing down. At this time, the cellophane tape specified in JIS Z1522 was used as the cellophane tape. The cellophane tape was fixed to the test table. Then, the stress when one end of the current collector was pulled vertically upward at a tensile speed of 50 mm / min and peeled off was measured. This measurement was performed three times, the average value was obtained, and the average value was taken as the peel strength (A) of the electrode.
- the IV resistance was measured as follows. Conditioning process that repeats the operation of charging at a charging rate of 0.1 C at a temperature of 25 ° C. until the voltage reaches 4.2 V, resting for 10 minutes, and then CC discharging to 3.0 V at a discharge rate of 0.1 C three times. was given. Then, in an atmosphere of -10 ° C, the battery is charged to 3.75V at 1C (C is a numerical value represented by the rated capacity (mA) / 1 hour (h)), and then 0.5C, 1 centering on 3.75V.
- a disper at 1000 rpm for 3 hours.
- -Preparation of cyclohexane solution of polymer 2 In a pressure resistant reactor, 233.3 kg of cyclohexane as an organic solvent, 54.2 mmol of N, N, N', N'-tetramethylethylenediamine (TMEDA), and an aromatic vinyl monomer 30.0 kg of styrene was added.
- TEDA N, N, N', N'-tetramethylethylenediamine
- cyclohexane in the obtained emulsion was distilled off under reduced pressure with a rotary evaporator to remove it. Then, the emulsion remaining after distilling off cyclohexane was centrifuged in a centrifuge (manufactured by Hitachi Koki Co., Ltd., "Himac CR21N") at 7000 rpm for 10 minutes, and then concentrated by taking out the upper layer portion. .. Then, ion-exchanged water is added to the upper layer portion so that the solid content concentration becomes 40% by mass, filtered through a 100-mesh wire mesh, and an aqueous dispersion containing polymer particles containing the polymer 1 and the polymer 2.
- the copper foil coated with the slurry composition for the negative electrode is conveyed at a rate of 400 mm / min in an oven at a temperature of 1200 ° C. for 2 minutes and further in an oven at a temperature of 130 ° C. for 2 minutes to obtain copper.
- the slurry composition on the foil was dried to obtain a negative electrode raw fabric in which a negative electrode mixture layer was formed on the current collector.
- the negative electrode mixture layer side of the prepared negative electrode raw fabric was roll-pressed in an environment of a temperature of 25 ⁇ 3 ° C. to obtain a negative electrode having a negative electrode mixture layer density of 1.60 g / cm 3.
- the peel strength of the negative electrode thus obtained was evaluated. The results are shown in Table 1.
- a planetary mixer contains 97 parts of NMC532 (Li [Ni 5/10 Co 2/10 Mn 3/10 ] O 2 ), a lithium composite oxide-based active material of Co—Ni—Mn as a positive electrode active material, and a conductive material.
- NMC532 Li [Ni 5/10 Co 2/10 Mn 3/10 ] O 2
- a lithium composite oxide-based active material of Co—Ni—Mn as a positive electrode active material
- a conductive material 1 part of acetylene black (manufactured by Denki Kagaku Kogyo Co., Ltd., product name "HS-100”) and 2 parts of polyvinylidene fluoride (manufactured by Kureha Co., Ltd., product name "# 7208”) as a binder (equivalent to solid content) was added and mixed.
- NMP N-methyl-2-pyrrolidone
- the obtained slurry composition for a positive electrode was applied with a comma coater on an aluminum foil having a thickness of 20 ⁇ m, which is a current collector, so that the coating amount was 20 ⁇ 0.5 mg / cm 2 . Further, the slurry composition on the aluminum foil is dried and collected by transporting the slurry composition on the aluminum foil at a speed of 200 mm / min in an oven having a temperature of 120 ° C. for 2 minutes and further in an oven having a temperature of 130 ° C. for 2 minutes. A positive electrode original fabric having a positive electrode mixture layer formed on it was obtained. Then, the positive electrode mixture layer side of the prepared positive electrode raw fabric was roll-pressed in an environment of a temperature of 25 ⁇ 3 ° C.
- a separator made of a separator base material a single-layer polypropylene separator (manufactured by Cellguard, product name "Cellguard 2500") was prepared.
- Cellguard 2500 a single-layer polypropylene separator
- a single-layer laminated cell (equivalent to an initial design discharge capacity of 30 mAh) was prepared using the above negative electrode, positive electrode, and separator, placed in an aluminum packaging material, and vacuum dried under the conditions of 60 ° C. and 10 hours. ..
- Example 2 When preparing the polymer particles, the compounding amount of the cyclohexane solution of the polymer 1 and the compounding amount of the cyclohexane solution of the polymer 2 to be mixed in the "preliminary mixing operation" are changed, respectively, to obtain the polymer in the polymer particles.
- Various operations, measurements, and evaluations were carried out in the same manner as in Example 1 except that the ratio of 1 was as shown in Table 1. The results are shown in Table 1.
- Example 4 When preparing a cyclohexane solution of polymer 1, maleic acid-modified SEBS (product name: Tuftec (registered trademark) M1911, acid value: 2 mgCH 3 ONa / g) manufactured by Asahi Kasei Co., Ltd. is used as polymer 1 having different acid values. Various operations, measurements, and evaluations were carried out in the same manner as in Example 1 except for the above. The results are shown in Table 1.
- Example 5 When preparing the cyclohexane solution of the polymer 1, various operations and measurements were carried out in the same manner as in Example 1 except that the prepared polymer 1 was used as the polymer 1 having a different acid value as follows. , And the evaluation was carried out. The results are shown in Table 1.
- Example 6 When preparing the cyclohexane solution of the polymer 1, various operations, measurements, and operations were carried out in the same manner as in Example 1 except that the polymer 1 prepared as follows was used as the polymer 1 having a different acid value. And evaluation was carried out. The results are shown in Table 1. ⁇ Preparation of polymer 1> A polymer was prepared in the same manner as in Example 5, except that the amount of maleic anhydride in Example 5 was changed from 7 parts to 18 parts. The acid value of the obtained polymer was measured and found to be 25 mgCH 3 ONa / g.
- Example 7 The same as in Example 1 except that 70.0 kg of isoprene was used instead of 70.0 kg of 1,3-butadiene as the aliphatic conjugated diene monomer when preparing the cyclohexane solution of the polymer 2. Various operations, measurements, and evaluations were carried out. The results are shown in Table 1.
- Example 8 Except for the fact that isoprene rubber (manufactured by Nippon Zeon Co., Ltd., "Nipol IR2200”) was used as the polymer 2 and dissolved in cyclohexane to prepare a cyclohexane solution of isoprene rubber having a concentration of 5.0% by mass. Various operations, measurements, and evaluations were carried out in the same manner as in Example 1. The results are shown in Table 1.
- Example 1 A cyclohexane solution of polymer 1, a cyclohexane solution of polymer 2, and an aqueous emulsifier solution having the same composition as in Example 1 were prepared in the same manner as in Example 1. Then, 500 g of the obtained cyclohexane solution of the polymer 1 and 700 g of the emulsifier aqueous solution were put into a tank, and an operation using a high-pressure emulsification disperser similar to the operation in the “pre-mixing operation” of Example 1 was performed. Then, in the subsequent operations in the same manner as in Example 1, an aqueous dispersion 1 containing polymer particles containing the polymer 1 (not containing the polymer 2) was obtained.
- the same operation was carried out for the cyclohexane solution of the polymer 2 to obtain an aqueous dispersion 2 containing the polymer particles containing the polymer 2 (not containing the polymer 1).
- the amount of polymer particles containing the polymer 1 (not including the polymer 2) is 0.75 parts in terms of solid content with respect to 97.5 parts of graphite.
- the aqueous dispersion 2 was added to the aqueous dispersion 1 so that the amount of the polymer particles containing the polymer 2 (not including the polymer 1) was 0.75 parts in the amount equivalent to the solid content. Except for these points, various operations, measurements, and evaluations were carried out in the same manner as in Example 1. The results are shown in Table 1.
- Example 2 A cyclohexane solution of polymer 2 and an aqueous emulsifier solution having the same composition as in Example 1 were prepared in the same manner as in Example 1. Then, 500 g of the obtained cyclohexane solution of the polymer 2 and 700 g of the emulsifier aqueous solution were put into a tank, and an operation using a high-pressure emulsification disperser similar to the operation in the "preliminary mixing operation" of Example 1 was performed. Then, in the subsequent operations, the same as in Example 1, an aqueous dispersion containing the polymer particles containing the polymer 2 (not containing the polymer 1) was obtained.
- the amount of the polymer particles containing the polymer 2 (not including the polymer 1) is 1.5 parts in the amount equivalent to the solid content with respect to 97.5 parts of graphite.
- the aqueous dispersion was added. No operation related to the polymer 1 was performed, and a slurry composition containing no polymer particles containing the polymer 1 was obtained. Except for these points, various operations, measurements, and evaluations were carried out in the same manner as in Example 1. The results are shown in Table 1.
- Example 3 A cyclohexane solution of polymer 1 and an aqueous emulsifier solution having the same composition as in Example 1 were prepared in the same manner as in Example 1. Then, 500 g of the obtained cyclohexane solution of the polymer 1 and 700 g of the emulsifier aqueous solution were put into a tank, and an operation using a high-pressure emulsification disperser similar to the operation in the “pre-mixing operation” of Example 1 was performed. Then, in the subsequent operations, the same as in Example 1, an aqueous dispersion containing the polymer particles containing the polymer 1 (not containing the polymer 2) was obtained.
- the amount of the polymer particles containing the polymer 1 (not including the polymer 2) is 1.5 parts in the amount equivalent to the solid content with respect to 97.5 parts of graphite.
- the aqueous dispersion was added. No operation related to the polymer 2 was performed, and a slurry composition containing no polymer particles containing the polymer 2 was obtained. Except for these points, various operations, measurements, and evaluations were carried out in the same manner as in Example 1. The results are shown in Table 1.
- M-SEBS represents a maleic anhydride-modified (styrene-ethylene / butylene-styrene) block polymer.
- ST indicates styrene
- SBS represents a (styrene-butadiene-styrene) block polymer
- SIS indicates a (styrene-isoprene-styrene) block polymer
- IR indicates an isoprene rubber.
- BT represents 1,3-butadiene units
- IP indicates an isoprene unit.
- the polymer 1 which is a block polymer having an acidic group-containing monomer unit and the aliphatic conjugated diene monomer unit which does not have an acidic group-containing monomer unit are 55% by mass or more.
- Comparative Examples 1 to 3 in which the type of the polymer contained in the polymer particles was one kind, it was not possible to provide both the slurry composition having excellent viscosity stability and the electrode having excellent peel strength. You can see that.
- a slurry composition for a non-aqueous secondary battery electrode having excellent viscosity stability and a binder composition for a non-aqueous secondary battery capable of forming an electrode for a non-aqueous secondary battery having excellent peel strength. can do.
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Abstract
Description
また、本発明は、ピール強度に優れる非水系二次電池用電極を形成可能であり、且つ、粘度安定性に優れる非水系二次電池電極用スラリー組成物を提供することを目的とする。
さらに、本発明は、ピール強度に優れる非水系二次電池用電極、及び、当該非水系二次電池用電極を備える非水系二次電池を提供することを目的とする。
なお、重合体の「単量体単位」とは、「その単量体を用いて得た重合体中に含まれる、当該単量体由来の繰り返し単位」を意味する。ここで、本発明において、重合体中の各繰り返し単位の「含有割合(質量%)」は、1H-NMRなどの核磁気共鳴(NMR)法を用いて測定することができる。
また、重合体1及び重合体2の合計質量を基準とした、重合体1の割合は、順相クロマトグラフィー等の電荷の差を利用して分離、定量する手法により測定することができる。
なお、「単量体単位からなるブロック領域を含む」とは、「ある重合体中に、繰り返し単位として、その単量体単位のみが連なって結合した部分が存在する」ことを意味する。
なお、重合体1の酸価は、実施例に記載した方法により測定することができる。
また、本発明によれば、ピール強度に優れる非水系二次電池用電極を形成可能であり、且つ、粘度安定性に優れる非水系二次電池電極用スラリー組成物を提供することができる。
さらに、本発明によれば、ピール強度に優れる非水系二次電池用電極、及び、当該非水系二次電池用電極を備える非水系二次電池を提供することができる。
ここで、本発明の非水系二次電池用バインダー組成物は、非水系二次電池の製造用途に用いられるものであり、特に、非水系二次電池の電極の製造用途に好適に用いることができる。例えば、本発明の非水系二次電池用バインダー組成物は、本発明の非水系二次電池電極用スラリー組成物の調製に用いることができる。そして、本発明のバインダー組成物を用いて調製したスラリー組成物は、リチウムイオン二次電池等の非水系二次電池の電極を製造する際に用いることができる。更に、本発明の非水系二次電池は、本発明のスラリー組成物を用いて形成した本発明の非水系二次電池用電極を用いたことを特徴とする。
なお、本発明の非水系二次電池用バインダー組成物、非水系二次電池電極用スラリー組成物及び非水系二次電池用電極は、負極用であることが好ましく、本発明の非水系二次電池は、本発明の非水系二次電池用電極を負極として用いたものであることが好ましい。
本発明のバインダー組成物は、所定の重合体粒子を含み、任意に、水などの溶媒、及び、バインダー組成物に配合され得るその他の成分を更に含有しうる。
そして、本発明のバインダー組成物は、重合体粒子が、酸性基含有単量体単位を有するブロック重合体である重合体1と、酸性基含有単量体単位を有さない重合体2と、を含み、重合体1及び重合体2の合計質量を基準として、重合体1の割合が10質量%以上90質量%以下であり、且つ、重合体2が、脂肪族共役ジエン単量体単位及びアルキレン構造単位の少なくとも一方を含み、重合体2に含まれる全繰り返し単位の合計質量を基準とした場合の、脂肪族共役ジエン単量体単位及びアルキレン構造単位の合計割合が、55質量%以上であることを特徴とする。このため、本発明のバインダー組成物によれば、粘度安定性に優れた非水系二次電池電極用スラリー組成物、及びピール強度に優れる非水系二次電池用電極を形成可能な非水系二次電池用バインダー組成物を提供することができる。
重合体粒子は、結着材として機能する成分であり、バインダー組成物を含むスラリー組成物を使用して電極合材層を形成した場合には、電極活物質などの成分が電極合材層から脱離しないように保持すると共に、電極合材層を集電体に対して密着させるとともに、電極合材層を介した電極とセパレータとの接着を可能としうる成分である。
そして、重合体粒子は、少なくとも重合体1及び重合体2を含有する非水溶性の粒子である。そして、重合体粒子は少なくとも重合体1及び重合体2を含み、各種重合体の調製段階及び重合体粒子の調製段階等において不可避的に混入する成分など、重合体1及び重合体2以外の成分を含んでいても良い。なお、本明細書において、粒子が「非水溶性」であるとは、温度25℃において粒子0.5gを100gの水に溶解した際に、不溶分が90質量%以上となることをいう。
重合体粒子に含まれる重合体1は、酸性基含有単量体単位を有するブロック重合体である。さらに、重合体1が、芳香族ビニル単量体単位からなるブロック領域(以下、「芳香族ビニルブロック領域1」と略記する場合がある。)を含む主鎖と、該主鎖に対して結合したグラフト部分とを有する重合体であり、主鎖に含まれる全繰り返し単位の合計質量を基準として、芳香族ビニル単量体単位の割合が10質量%以上50質量%以下であり、且つ、グラフト部分に酸性基含有単量体単位を含む重合体であることが好ましい。このように、重合体1の主鎖における芳香族ビニル単量体単位の割合が10質量%以上50質量%以下であれば、バインダー組成物を用いて形成した電極のピール強度を向上させることができるとともに、得られる二次電池の内部抵抗を低減することができる。また、酸性基含有単量体単位が重合体1のグラフト部分に含有されていれば、得られるスラリー組成物の粘度安定性を一層高めることができる。
芳香族ビニルブロック領域1は、上述したように、繰り返し単位として、芳香族ビニル単量体単位のみを含む領域である。
ここで、1つの芳香族ビニルブロック領域1は、1種の芳香族ビニル単量体単位のみで構成されていてもよいし、複数種の芳香族ビニル単量体単位で構成されていてもよいが、1種の芳香族ビニル単量体単位のみで構成されていることが好ましい。
また、1つの芳香族ビニルブロック領域1には、カップリング部位が含まれていてもよい(すなわち、1つの芳香族ビニルブロック領域を構成する芳香族ビニル単量体単位は、カップリング部位が介在して連なっていてもよい)。
そして、重合体1が複数の芳香族ビニルブロック領域1を有する場合、それら複数の芳香族ビニルブロック領域1を構成する芳香族ビニル単量体単位の種類及び割合は、同一でも異なっていてもよいが、同一であることが好ましい。
なお、芳香族ビニル単量体単位が重合体1の主鎖中に占める割合は、通常、芳香族ビニルブロック領域1が重合体1の主鎖中に占める割合と一致する。
その他の領域は、上述したように、繰り返し単位として、芳香族ビニル単量体単位以外の繰り返し単位(以下、「その他の繰り返し単位」と略記する場合がある。)のみを含む領域である。
ここで、1つのその他の領域は、1種のその他の繰り返し単位で構成されていてもよいし、複数種のその他の繰り返し単位で構成されていてもよい。
また、1つのその他の領域には、カップリング部位が含まれていてもよい(すなわち、1つのその他の領域を構成するその他の繰り返し単位は、カップリング部位が介在して連なっていてもよい)。
そして、重合体1が複数のその他の領域を有する場合、それら複数のその他の領域を構成するその他の繰り返し単位の種類及び割合は、同一でも異なっていてもよい。
ここで、その他の領域を構成する脂肪族共役ジエン単量体単位を形成し得る脂肪族共役ジエン単量体としては、例えば、1,3-ブタジエン、2-メチル-1,3-ブタジエン(イソプレン)、2,3-ジメチル-1,3-ブタジエン、2-クロル-1,3-ブタジエン;主鎖において共役二重結合を有するペンタジエン及びその置換体;並びに、側鎖において共役二重結合を有するヘキサジエン及びその置換体;等が挙げられる。これらは1種を単独で、又は、2種以上を組み合わせて用いることができる。
また、その他の領域を構成するアルキレン構造単位は、一般式:-CnH2n-[但し、nは2以上の整数]で表わされるアルキレン構造のみで構成される繰り返し単位である。例えば、アルキレン構造単位の炭素数は、例えば8以下、好ましくは6以下であり得る。
ここで、アルキレン構造単位は、直鎖状であっても分岐状であってもよい。
なお、重合体1は、グラフト部分を含んでいることが好ましい。より詳細には、重合体1が、繰り返し単位として酸性基含有単量体単位を含むグラフト部分を含んでいることが好ましい。なお、グラフト部分の重合体1の主鎖に対する結合位置は、特に限定されないが、重合体1が[芳香族ビニルブロック領域1]及び[脂肪族共役ジエン単量体単位及びアルキレン構造単位の少なくとも一方を含むその他の領域]を含む場合には、グラフト部分は、[その他の領域]に対して結合され得る。重合体1が、グラフト部分に酸性基含有単量体単位を含んでいれば、重合体粒子の表層付近における酸性基含有単量体単位の頻度が、重合体粒子の内部よりも高まる。これにより、水などの溶媒中における、重合体粒子の粒子安定性及び分散安定性を高めることができる。
モノカルボン酸としては、アクリル酸、メタクリル酸、クロトン酸などが挙げられる。
モノカルボン酸誘導体としては、2-エチルアクリル酸、イソクロトン酸、α-アセトキシアクリル酸、β-trans-アリールオキシアクリル酸、α-クロロ-β-E-メトキシアクリル酸などが挙げられる。
ジカルボン酸としては、マレイン酸、フマル酸、イタコン酸などが挙げられる。
ジカルボン酸誘導体としては、メチルマレイン酸、ジメチルマレイン酸、フェニルマレイン酸、クロロマレイン酸、ジクロロマレイン酸、フルオロマレイン酸や、マレイン酸ノニル、マレイン酸デシル、マレイン酸ドデシル、マレイン酸オクタデシル、マレイン酸フルオロアルキルなどのマレイン酸モノエステルが挙げられる。
ジカルボン酸の酸無水物としては、無水マレイン酸、アクリル酸無水物、メチル無水マレイン酸、ジメチル無水マレイン酸などが挙げられる。
また、カルボキシル基含有単量体としては、加水分解によりカルボキシル基を生成する酸無水物も使用できる。
なお、本発明において、「(メタ)アリル」とは、アリル及び/又はメタリルを意味する。
なお、本発明において、「(メタ)アクリロイル」とは、アクリロイル及び/又はメタクリロイルを意味する。
重合体1は、酸価が、0.5mgCH3ONa/g以上であることが好ましく、2.0mgCH3ONa/g以上であることがより好ましく、5.0mgCH3ONa/g以上であることがさらに好ましく、30mgCH3ONa/g以下であることが好ましく、20mgCH3ONa/g以下であることがより好ましく、12mgCH3ONa/g以下であることがさらに好ましい。重合体1の酸価が、上記下限値以上であれば、重合体粒子の安定性を高めることができ、得られるスラリー組成物の粘度安定性を一層高めることができる。さらに、重合体1の酸価が、上記下限値以上であれば、得られる電極のピール強度も高めることができる。また、重合体1の酸価が上記上限値以下であれば、重合体粒子の柔軟性を高めることができる。これにより、電極を形成した場合の、集電体と電極合材層との間を、より良好に密着させることが可能となり、電極のピール強度を一層高めることができる。さらに、重合体の酸価値が上記上限値以下であれば、得られる二次電池の内部抵抗を一層低減することができる。なお、重合体1の酸価の値は、重合体1の有する酸性基含有単量体単位の量を示す。重合体1を調製する場合に、グラフト重合の際に添加する酸性基含有単量体及び重合開始剤の量、並びに重合時間などを適宜調節することにより、所望の酸価の重合体1を得ることができる。
重合体1は、例えば、有機溶媒中にて、第一の単量体成分を重合させた溶液に、第一の単量体成分とは異なる第二の単量体成分を加えて重合を行い、必要に応じて、単量体成分の添加と重合とを更に繰り返すことより、調製することができる。なお、反応溶媒として使用される有機溶媒も特に限定されず、単量体の種類等に応じて適宜選択することができる。なお、ブロック重合体である重合体1の調製にあたり、カップリング剤を用いたカップリング反応に供してもよい。カップリング反応を行えば、例えば、ブロック重合体中に含まれるジブロック構造体同士の末端をカップリング剤により結合させて、トリブロック構造体に変換することができる。なお、カップリング反応に使用し得るカップリング剤としては、特に限定されず、例えば、既知の、2官能以上の多官能のカップリング剤が挙げられる。
重合体粒子に含まれる重合体2は、酸性基含有単量体単位を含まない。酸性基含有単量体単位については、重合体1について上述した通りであり、重合体2はかかる酸性基含有単量体単位を含まないことを特徴とする。さらに、重合体2は、脂肪族共役ジエン単量体単位及びアルキレン構造単位の少なくとも一方を含み、且つ、重合体2に含まれる全繰り返し単位の合計質量を基準(100質量%)とした場合の、脂肪族共役ジエン単量体単位及びアルキレン構造単位の合計割合が、55質量%以上である、重合体である。なお、重合体粒子が重合体2に相当する成分を、一種のみならず複数種含むこともありうる。さらに、重合体2は、特に限定されることなく、ランダム重合体又はブロック重合体であり得るが、中でも、ブロック重合体であることが好ましい。重合体粒子が重合体2として所定のブロック重合体を含んでいれば、得られる電極のピール強度を一層向上させることができる。
重合体2は、任意で、上記以外にその他の単位を有していてもよい。かかる単位としては、重合体1について上述したような、芳香族ビニル単量体単位、及びα,β-不飽和ニトリル単量体単位が挙げられる。なお、重合体2がブロック重合体である場合には、脂肪族共役ジエン単量体単位及びアルキレン構造単位の少なくとも一方を含むブロック領域に加えて、重合体2が芳香族ビニル単量体単位より成るブロック領域(以下、「芳香族ビニルブロック領域2」と略記する場合がある。)を有することが好ましい。芳香族ビニルブロック領域2については、重合体1の芳香族ビニルブロック領域1について詳述した内容と同様である。重合体2が芳香族ビニルブロック領域2を含んでいれば、得られる電極のピール強度を一層高めることができる。
バインダー組成物中に含まれる重合体粒子において、上述した重合体1及び重合体2の合計質量を基準(100質量%)として、重合体1の割合が、10質量%以上である必要があり、20質量%以上であることが好ましく、30質量%以上であることがより好ましく、90質量%以下である必要があり、80質量%以下であることがより好ましく、70質量%以下であることがさらに好ましい。重合体1の割合が上記下限値以上であれば、スラリー組成物中における重合体粒子の安定性を高めることができ、スラリー組成物の粘度安定性を高めることができる。また、重合体1の割合が上記上限値以下であれば、得られる電極のピール強度を高めることができる。
重合体粒子は、既知の添加剤を含んでいてもよい。このような既知の添加剤としては、例えば、酸化防止剤等が挙げられる。そして、酸化防止剤としては、特に限定されることなく、例えば、4-[[4,6-ビス(オクチルチオ)-1,3,5-トリアジン-2-イル]アミノ]-2,6-ジ-tert-ブチルフェノール等のヒンダードフェノール系酸化防止剤;3,9-ビス(オクタデシルオキシ)-2,4,8,10-テトラオキサ-3,9-ジホスファスピロ[5.5]ウンデカン等のホスファイト系酸化防止剤;などが挙げられる。
上述した重合体1及び重合体2を含む重合体粒子の調製方法は特に限定されない。例えば、上記所定の重合体粒子は、重合体1、重合体2、有機溶媒、乳化剤、及び水を含む予備混合物を得る工程(予備混合工程)と、得られた予備混合物を転相乳化する転相乳化工程と、を経て容易に調製することができる。
予備混合工程では、重合体1、重合体2、有機溶媒、乳化剤、及び水を含む予備混合物を得る。かかる予備混合物を得るための手順は特に限定されない。例えば、重合体1及び重合体2の双方を、有機溶媒に対して溶解した状態としてから、これらと、乳化剤及び水を混合することで、予備混合物を得ることができる。
転相乳化工程における転相乳化の方法は、特に限定されないが、例えば、上述した予備混合工程で得られた予備混合物を乳化分散機を用いて転相乳化することができる。具体的には、乳化分散機としては、特に限定されることなく、例えば、商品名「ホモジナイザー」(IKA社製)、商品名「ポリトロン」(キネマティカ社製)、商品名「TKオートホモミキサー」(特殊機化工業社製)等のバッチ式乳化分散機;商品名「TKパイプラインホモミキサー」(特殊機化工業社製)、商品名「コロイドミル」(神鋼パンテック社製)、商品名「スラッシャー」(日本コークス工業社製)、商品名「トリゴナル湿式微粉砕機」(三井三池化工機社製)、商品名「キャビトロン」(ユーロテック社製)、商品名「マイルダー」(太平洋機工社製)、商品名「ファインフローミル」(太平洋機工社製)等の連続式乳化分散機;商品名「マイクロフルイダイザー」(みずほ工業社製)、商品名「ナノマイザー」(ナノマイザー社製)、商品名「APVガウリン」(ガウリン社製)、「LAB1000」(SPXFLOW社製)等の高圧乳化分散機;商品名「膜乳化機」(冷化工業社製)等の膜乳化分散機;商品名「バイブロミキサー」(冷化工業社製)等の振動式乳化分散機;商品名「超音波ホモジナイザー」(ブランソン社製)等の超音波乳化分散機;などを用いることができる。なお、乳化分散機による乳化操作の条件(例えば、処理温度、処理時間など)は、特に限定されず、所望の分散状態になるように適宜選定すればよい。
そして、転相乳化後に得られる乳化液から、必要に応じて、既知の方法により有機溶媒を除去する等して、重合体1及び重合体2を含む重合体粒子の水分散液を得ることができる。
本発明のバインダー組成物は、上記成分以外の成分(その他の成分)を含有することができる。例えば、バインダー組成物は、上述した重合体粒子以外の、既知の粒子状結着材(スチレンブタジエンランダム共重合体、アクリル重合体など)を含んでいてもよい。
また、バインダー組成物は、既知の添加剤を含んでいてもよい。このような既知の添加剤としては、例えば、重合体粒子に含まれうる添加剤として上記に挙げた添加剤、さらには、消泡剤、分散剤、増粘剤等が挙げられる。
さらに、バインダー組成物は、溶媒としての水と、少量の有機溶媒とを任意で含み得る。かかる有機溶媒は、重合体粒子を製造する際に用いた有機溶媒の残留物であってもよい。
なお、その他の成分は、1種を単独で用いてもよく、2種以上を任意の比率で組み合わせて用いてもよい。
本発明のバインダー組成物の製造方法は、上述した重合体粒子の調製方法に従って重合体粒子を調製することを含む。すなわち、本発明のバインダー組成物の製造方法は、上記の予備混合工程と、転相乳化工程とを少なくとも含む。そして、本発明のバインダー組成物の製造方法は、転相乳化工程を経て得られた、重合体1及び重合体2を含む重合体粒子の水分散液に対して、任意で、所望の添加剤等を添加する工程をさらに含みうる。
本発明のスラリー組成物は、電極の電極合材層の形成用途に用いられる組成物であり、上述したバインダー組成物を含み、電極活物質を更に含有する。即ち、本発明のスラリー組成物は、上述した重合体粒子、電極活物質を含有し、任意に、溶媒としての水及びその他の成分を更に含有する。そして、本発明のスラリー組成物は、上述したバインダー組成物を含んでいるので、粘度安定性に優れている。また、本発明のスラリー組成物を用いれば、ピール強度に優れる電極を形成可能である。
バインダー組成物としては、上述した本発明のバインダー組成物を用いる。
なお、スラリー組成物中のバインダー組成物の配合量は、特に限定されない。例えば、バインダー組成物の配合量は、電極活物質100質量部当たり、固形分換算で、重合体粒子の量が0.5質量部以上15質量部以下となる量とすることができる。
そして、電極活物質としては、特に限定されることなく、二次電池に用いられる既知の電極活物質を使用することができる。具体的には、例えば、二次電池の一例としてのリチウムイオン二次電池の電極合材層において使用し得る電極活物質としては、特に限定されることなく、以下の電極活物質を用いることができる。
リチウムイオン二次電池の正極の正極合材層に配合される正極活物質としては、例えば、遷移金属を含有する化合物、例えば、遷移金属酸化物、遷移金属硫化物、リチウムと遷移金属との複合金属酸化物などを用いることができる。なお、遷移金属としては、例えば、Ti、V、Cr、Mn、Fe、Co、Ni、Cu、Mo等が挙げられる。
具体的には、正極活物質としては、特に限定されることなく、リチウム含有コバルト酸化物(LiCoO2)、マンガン酸リチウム(LiMn2O4)、リチウム含有ニッケル酸化物(LiNiO2)、Li[Ni5/10Co2/10Mn3/10]O2等のCo-Ni-Mnのリチウム含有複合酸化物、Ni-Mn-Alのリチウム含有複合酸化物、Ni-Co-Alのリチウム含有複合酸化物、オリビン型リン酸鉄リチウム(LiFePO4)、オリビン型リン酸マンガンリチウム(LiMnPO4)、Li1+xMn2-xO4(0<X<2)で表されるリチウム過剰のスピネル化合物、Li[Ni0.17Li0.2Co0.07Mn0.56]O2、LiNi0.5Mn1.5O4等が挙げられる。
なお、上述した正極活物質は、1種類を単独で使用してもよいし、2種類以上を組み合わせて用いてもよい。
リチウムイオン二次電池の負極の負極合材層に配合される負極活物質としては、例えば、炭素系負極活物質、金属系負極活物質、及び、これらを組み合わせた負極活物質などが挙げられる。
ここで、炭素系負極活物質とは、リチウムを挿入(「ドープ」ともいう。)可能な、炭素を主骨格とする活物質をいう。そして、炭素系負極活物質としては、具体的には、コークス、メソカーボンマイクロビーズ(MCMB)、メソフェーズピッチ系炭素繊維、熱分解気相成長炭素繊維、フェノール樹脂焼成体、ポリアクリロニトリル系炭素繊維、擬等方性炭素、フルフリルアルコール樹脂焼成体(PFA)及びハードカーボンなどの炭素質材料、並びに、天然黒鉛(グラファイト)及び人造黒鉛などの黒鉛質材料が挙げられる。
また、金属系負極活物質とは、金属を含む活物質であり、通常は、リチウムの挿入が可能な元素を構造に含み、リチウムが挿入された場合の単位質量当たりの理論電気容量が500mAh/g以上である活物質をいう。そして、金属系活物質としては、例えば、リチウム金属、リチウム合金を形成し得る単体金属(例えば、Ag、Al、Ba、Bi、Cu、Ga、Ge、In、Ni、P、Pb、Sb、Si、Sn、Sr、Zn、Tiなど)及びそれらの酸化物、硫化物、窒化物、ケイ化物、炭化物、燐化物などが挙げられる。さらに、チタン酸リチウムなどの酸化物を挙げることができる。
なお、上述した負極活物質は、1種類を単独で使用してもよいし、2種類以上を組み合わせて用いてもよい。
スラリー組成物に配合し得るその他の成分としては、特に限定することなく、導電材や、本発明のバインダー組成物に配合し得るその他の成分と同様のものが挙げられる。なお、その他の成分は、1種類を単独で用いてもよく、2種類以上を任意の比率で組み合わせて用いてもよい。
スラリー組成物の調製方法は、特に限定はされない。
例えば、バインダー組成物と、電極活物質と、必要に応じて用いられるその他の成分とを、水系媒体の存在下で混合してスラリー組成物を調製することができる。
なお、スラリー組成物の調製の際に用いる水などの溶媒には、バインダー組成物に含まれていたものも含まれる。また、混合方法は特に制限されないが、通常用いられうる攪拌機や、分散機を用いて混合することができる。
本発明の非水系二次電池用電極は、上述した非水系二次電池電極用スラリー組成物を用いて形成した電極合材層を備える。したがって、電極合材層は、上述したスラリー組成物の乾燥物よりなり、通常、電極活物質と、重合体粒子に由来する成分と、を含有し、任意に、その他の成分を含有する。なお、電極合材層中に含まれている各成分は、上記非水系二次電池電極用スラリー組成物中に含まれていたものであり、それら各成分の好適な存在比は、スラリー組成物中の各成分の好適な存在比と同じである。また、重合体粒子は、スラリー組成物中では粒子形状で存在するが、スラリー組成物を用いて形成された電極合材層中では、粒子形状であってもよいし、その他の任意の形状であってもよい。
そして、本発明の非水系二次電池用電極は、上述した非水系二次電池電極用スラリー組成物を使用して電極合材層を形成しているので、ピール強度に優れている。
ここで、本発明の非水系二次電池用電極の電極合材層は、例えば、以下の方法を用いて形成することができる。
1)本発明のスラリー組成物を集電体の表面に塗布し、次いで乾燥する方法;
2)本発明のスラリー組成物に集電体を浸漬後、これを乾燥する方法;及び
3)本発明のスラリー組成物を離型基材上に塗布し、乾燥して電極合材層を製造し、得られた電極合材層を集電体の表面に転写する方法。
これらの中でも、前記1)の方法が、電極合材層の層厚制御をしやすいことから特に好ましい。前記1)の方法は、詳細には、スラリー組成物を集電体上に塗布する工程(塗布工程)と、集電体上に塗布されたスラリー組成物を乾燥させて集電体上に電極合材層を形成する工程(乾燥工程)を含む。
上記スラリー組成物を集電体上に塗布する方法としては、特に限定されず公知の方法を用いることができる。具体的には、塗布方法としては、ドクターブレード法、ディップ法、リバースロール法、ダイレクトロール法、グラビア法、エクストルージョン法、ハケ塗り法などを用いることができる。この際、スラリー組成物を集電体の片面だけに塗布してもよいし、両面に塗布してもよい。塗布後乾燥前の集電体上のスラリー膜の厚みは、乾燥して得られる電極合材層の厚みに応じて適宜に設定しうる。
集電体上のスラリー組成物を乾燥する方法としては、特に限定されず公知の方法を用いることができ、例えば温風、熱風、低湿風による乾燥法、真空乾燥法、赤外線や電子線などの照射による乾燥法を用いることができる。このように集電体上のスラリー組成物を乾燥することで、集電体上に電極合材層を形成し、集電体と電極合材層とを備える非水系二次電池用電極を得ることができる。
本発明の非水系二次電池は、正極と、負極と、電解液と、セパレータとを備えており、上述した非水系二次電池用電極を正極及び負極の少なくとも一方として用いる。そして、本発明の非水系二次電池は、上述した非水系二次電池用電極を正極及び負極の少なくとも一方として用いて製造されるため、優れた電池特性を発揮し得る。
なお、以下では、一例として非水系二次電池がリチウムイオン二次電池である場合について説明するが、本発明は下記の一例に限定されるものではない。
ここで、本発明の非水系二次電池で使用し得る、上述した本発明の非水系二次電池用電極以外の電極としては、特に限定されることなく、二次電池の製造に用いられている既知の電極を用いることができる。具体的には、上述した本発明の非水系二次電池用電極以外の電極としては、既知の製造方法を用いて集電体上に電極合材層を形成してなる電極などを用いることができる。
電解液としては、通常、有機溶媒に支持電解質を溶解した有機電解液が用いられる。リチウムイオン二次電池の支持電解質としては、例えば、リチウム塩が用いられる。リチウム塩としては、例えば、LiPF6、LiAsF6、LiBF4、LiSbF6、LiAlCl4、LiClO4、CF3SO3Li、C4F9SO3Li、CF3COOLi、(CF3CO)2NLi、(CF3SO2)2NLi、(C2F5SO2)NLiなどが挙げられる。なかでも、溶媒に溶けやすく高い解離度を示すので、LiPF6、LiClO4、CF3SO3Liが好ましい。なお、電解質は1種類を単独で用いてもよく、2種類以上を任意の比率で組み合わせて用いてもよい。通常は、解離度の高い支持電解質を用いるほどリチウムイオン伝導度が高くなる傾向があるので、支持電解質の種類によりリチウムイオン伝導度を調節することができる。
なお、電解液中の電解質の濃度は適宜調整することができる。また、電解液には、既知の添加剤を添加することができる。
セパレータとしては、特に限定されることなく、例えば特開2012-204303号公報に記載のものを用いることができる。これらの中でも、セパレータ全体の膜厚を薄くすることができ、これにより、二次電池内の電極活物質の比率を高くして体積あたりの容量を高くすることができるという点より、ポリオレフィン系(ポリエチレン、ポリプロピレン、ポリブテン、ポリ塩化ビニル)の樹脂からなる微多孔膜が好ましい。
そして、実施例及び比較例において、各種の性状の測定、及び各種の評価は、以下に従って実施した。
実施例、比較例で用いた重合体を、測定試料とした。1H-NMRにより、測定試料が含有する芳香族ビニル単量体単位、脂肪族共役ジエン単量体単位、及び酸性基含有単量体単位のそれぞれに由来するピークの強度を算出した。そして、全ピーク強度に対する各単量体単位に由来するピーク強度の割合を、測定試料である重合体中の当該各単量体単位の割合とした。
<重合体1の酸価>
重合体1を、90℃、1時間の条件にて乾燥させた。次に乾燥した重合体1を0.05g秤量し、トルエン50mLに室温で溶解させた後、これにエタノール10mLをさらに加えて混合し、ポリマー溶液を調製した。次に、電位差自動滴定装置(京都電子工業株式会社製、AT610)を用い、電位差滴定を行なった。滴定液には0.05mol/Lナトリウムメトキシド/メタノール溶液(校正係数f=1.012)を用いた。指示電極にはガラス電極、比較電極には液絡部がスリーブ型のもの(内部液:1M LiCl/エタノール溶液)を用いた。滴定の終点までに有した、重合体1gに対するナトリウムメトキシド重量を酸価とした。
B型粘度計(東機産業社製、製品名「TVB-10」、回転数:60rpm)を用いて、得られたスラリー組成物の粘度η0を測定した。次に、粘度を測定したスラリー組成物を、プラネタリーミキサー(回転数:60rpm)を用いて24時間攪拌し、攪拌後のスラリー組成物の粘度η1を、上記と同様のB型粘度計(回転数:60rpm)を用いて測定した。そして、攪拌前後のスラリー組成物の粘度変化率Δη={(η0-η1)/η0}×100(%)を算出し、以下の基準にてスラリー組成物の粘度安定性を評価した。なお、粘度測定時の温度は25℃であった。粘度変化率の絶対値|Δη|の値が0に近いほど、スラリー組成物の粘度安定性が優れていることを示す。
A:粘度変化率の絶対値|Δη|が0%以上10%未満
B:粘度変化率の絶対値|Δη|が10%以上20%未満
C:粘度変化率の絶対値|Δη|が20%以上30%未満
D:粘度変化率の絶対値|Δη|が30%以上
作製した負極を長さ100mm、幅10mmの長方形に切り出して試験片とした。この試験片を、負極合材層の表面を下にして、負極合材層の表面にセロハンテープを貼り付けた。この際、セロハンテープとしてはJIS Z1522に規定されるセロハンテープを用いた。また、セロハンテープは試験台に固定しておいた。その後、集電体の一端を鉛直上方に引張り速度50mm/分で引っ張って剥がしたときの応力を測定した。この測定を3回行い、その平均値を求めて、当該平均値を電極のピール強度(A)とした。そして、下記の基準により評価を行なった。ピール強度が大きいほど、負極合材層の集電体に対する結着力が大きいこと、すなわち、密着強度が大きいことを示す。
A:10N/m以上
B:7N/m以上10N/m未満
C:5N/m以上7N/m未満
D:5N/m未満
リチウムイオン二次電池の内部抵抗を評価するために、以下のようにしてIV抵抗を測定した。温度25℃で、電圧が4.2Vとなるまで0.1Cの充電レートで充電し、10分間休止した後、0.1Cの放電レートで3.0VまでCC放電させる操作を3回繰り返すコンディショニング処理を施した。その後、-10℃雰囲気下で、1C(Cは定格容量(mA)/1時間(h)で表される数値)で3.75Vまで充電した後、3.75Vを中心として0.5C、1.0C、1.5C、2.0Cで、20秒間充電と20秒間放電とをそれぞれ行った。そして、それぞれの場合について、充電側における15秒後の電池電圧を電流値に対してプロットし、その傾きをIV抵抗(Ω)として求めた。得られたIV抵抗の値(Ω)について、下記の基準により評価を行なった。なお、IV抵抗の値が小さいほど、二次電池の内部抵抗が低いことを示す。
A:2.0Ω未満
B:2.0Ω以上2.3Ω未満
C:2.3Ω以上2.5Ω未満
D:2.5Ω以上
<非水系二次電池用バインダー組成物の調製>
1.重合体粒子の調製
1-1.予備混合工程
・重合体1のシクロヘキサン溶液の調製
有機溶媒としてのシクロヘキサンに、マレイン酸変性SEBS(無水マレイン酸変性の(スチレン-エチレン・ブチレン-スチレン)ブロック重合体;旭化成社製;「タフテック(登録商標)M1913」;酸価:10mgCH3ONa/g;スチレン単位:30質量%;エチレン単位・ブチレン単位の合計:70質量%)を、固形分濃度5.0質量%になるように添加し、ディスパーで1000rpm、3時間攪拌して、酸性基含有単量体単位を有するブロック重合体である重合体1のシクロヘキサン溶液を調製した。
・重合体2のシクロヘキサン溶液の調製
耐圧反応器に、有機溶媒としてのシクロヘキサン233.3kg、N,N,N’,N’-テトラメチルエチレンジアミン(TMEDA)54.2mmol、及び芳香族ビニル単量体としてのスチレン30.0kgを添加した。そしてこれらを40℃で攪拌しているところに、重合開始剤としてのn-ブチルリチウム1806.5mmolを添加し、50℃に昇温しながら1時間重合した。スチレンの重合転化率は100%であった。引き続き、50~60℃を保つように温度制御しながら、耐圧反応器に、脂肪族共役ジエン単量体としての1,3-ブタジエン70.0kgを1時間にわたり連続的に添加した。1,3-ブタジエンの添加を完了後、重合反応を更に1時間継続した。1,3-ブタジエンの重合転化率は100%であった。次いで、耐圧反応器に、カップリング剤としてのジクロロジメチルシラン722.6mmolを添加して2時間カップリング反応を行い、スチレン-ブタジエンカップリングブロック共重合体を形成させた。その後、活性末端を失活させるべく、反応液にメタノール3612.9mmolを添加してよく混合した。次いで、この反応液100部(重合体成分を30.0部含有)に、ヒンダードフェノール系酸化防止剤としての4-[[4,6-ビス(オクチルチオ)-1,3,5-トリアジン-2-イル]アミノ]-2,6-ジ-tert-ブチルフェノール0.05部、及び、ホスファイト系酸化防止剤としての3,9-ビス(オクタデシルオキシ)-2,4,8,10-テトラオキサ-3,9-ジホスファスピロ[5.5]ウンデカン0.09部を加えて混合した。得られた混合溶液を、85~95℃の温水中に少しずつ滴下することで溶媒を揮発させて、析出物を得た。そして、この析出物を粉砕し、85℃で熱風乾燥することにより、酸性基含有単量体単位を有さない、脂肪族共役ジエン単量体単位の含有割合が70質量%であるブロック重合体である重合体2を含む乾燥物を回収した。
そして、回収した乾燥物をシクロヘキサンに溶解し、重合体2の濃度が5.0質量%である重合体2のシクロヘキサン溶液を調製した。
・乳化剤水溶液の調製
アルキルベンゼンスルホン酸ナトリウムをイオン交換水に溶解し、0.15質量%の乳化剤水溶液を調製した。
・予備混合操作
そして、上記で得られた、重合体1のシクロヘキサン溶液500gと、重合体2のシクロヘキサン溶液500gと、乳化剤水溶液1400gとを、タンク内に投入し、攪拌させることで予備混合を行い、予備混合物を得た。続いて、得られた予備混合物を、定量ポンプを用いて、タンク内から高圧乳化分散機(SPXFLOW社製、「LAB1000」)へと移送し、高圧乳化分散機内の流路を循環することにより(パス回数:5回)、予備混合物を転相乳化した乳化液を得た。
次に、得られた乳化液中のシクロヘキサンをロータリーエバポレータにて減圧留去して除去した。その後、シクロヘキサンを留去した後に残った乳化液を、遠心分離機(日立工機社製、「Himac CR21N」)にて、7000rpmで10分間遠心した後、上層部分を取り出すことで濃縮を行った。
その後、上層部分に固形分濃度が40質量%になるようにイオン交換水を添加した後、100メッシュの金網で濾過し、重合体1及び重合体2を含む重合体粒子を含有する水分散液を得た。
<非水系二次電池負極用スラリー組成物の調製>
プラネタリーミキサーに、負極活物質としてのグラファイト(天然黒鉛)(容量:360mAh/g)97.5部と、増粘剤としてのカルボキシメチルセルロース(CMC)1部(固形分相当)とを投入して混合物を得た。さらに、得られた混合物をイオン交換水で固形分濃度60%に調整した後、回転速度45rpmで60分間混練した。その後、上述で調製されたバインダー組成物を重合体粒子の固形分相当量で1.5部投入し、回転速度40rpmで40分間混練した。そして、粘度(B型粘度計を用い、温度:25℃、ローター回転数:60rpmにて測定)が3000±500mPa・sとなるようにイオン交換水を加えることにより、負極用スラリー組成物を得た。
得られた負極用スラリー組成物の粘度安定性を評価した。結果を表1に示す。
<負極の形成>
得られた負極用スラリー組成物を、コンマコーターで、集電体である厚さ15μmの電解銅箔の上に、塗布量が11±0.5mg/cm2になるように塗布した。その後、負極用スラリー組成物が塗布された銅箔を、400mm/分の速度で、温度1200℃のオーブン内を2分間、さらに温度130℃のオーブン内を2分間かけて搬送することにより、銅箔上のスラリー組成物を乾燥させ、集電体上に負極合材層が形成された負極原反を得た。
その後、作製した負極原反の負極合材層側を温度25±3℃の環境下でロールプレスし、負極合材層密度が1.60g/cm3の負極を得た。このようして得られた負極のピール強度を評価した。結果を表1に示す。
<正極の形成>
プラネタリーミキサーに、正極活物質としてのCo-Ni-Mnのリチウム複合酸化物系の活物質NMC532(Li[Ni5/10Co2/10Mn3/10]O2)97部と、導電材としてのアセチレンブラック(電気化学工業社製、製品名「HS-100」)1部と、結着材としてのポリフッ化ビニリデン(クレハ社製、製品名「#7208」)2部(固形分相当)を添加し、混合した。さらに、有機溶媒としてのN-メチル-2-ピロリドン(NMP)を徐々に加えて、温度25±3℃、回転数25rpmにて攪拌混合して、粘度(B型粘度計を用い、温度:25±3℃、ローター:M4、ローター回転数:60rpmにて測定)が3600mPa・sである正極用スラリー組成物を得た。
得られた正極用スラリー組成物を、コンマコーターで、集電体である厚さ20μmのアルミ箔の上に、塗布量が20±0.5mg/cm2となるように塗布した。さらに、200mm/分の速度で、温度120℃のオーブン内を2分間、さらに温度130℃のオーブン内を2分間かけて搬送することにより、アルミニウム箔上のスラリー組成物を乾燥させ、集電体上に正極合材層が形成された正極原反を得た。
その後、作製した正極原反の正極合材層側を温度25±3℃の環境下でロールプレスし、正極合材層密度が3.20g/cm3の正極を得た。
<セパレータの準備>
セパレータ基材よりなるセパレータとして、単層のポリプロピレン製セパレータ(セルガード社製、製品名「セルガード2500」)を準備した。
<リチウムイオン二次電池の作製>
上記の負極及び正極、セパレータを用いて、単層ラミネートセル(初期設計放電容量30mAh相当)を作製し、アルミ包材内に配置して、60℃、10時間の条件にて真空乾燥をおこなった。その後、電解液として濃度1.0MのLiPF6溶液(溶媒:エチレンカーボネート(EC)/ジエチルカーボネート(DEC)=5/5(体積比)の混合溶媒、添加剤:ビニレンカーボネート2体積%(溶媒比)を含有)を充填した。さらに、アルミ包材の開口を密封するために、温度150℃のヒートシールをしてアルミ包材を閉口し、リチウムイオン二次電池を製造した。このリチウムイオン二次電池を用いて、内部抵抗を評価した。結果を表1に示す。
重合体粒子を調製するに際して、「予備混合操作」において混合する重合体1のシクロヘキサン溶液の配合量、及び重合体2のシクロヘキサン溶液の配合量をそれぞれ変更して、得られる重合体粒子における重合体1の比率が表1に示す通りとなるようにした以外は、実施例1と同様にして、各種操作、測定、及び評価を実施した。結果を表1に示す。
重合体1のシクロヘキサン溶液を調製する際に、酸価の異なる重合体1として、旭化成社製マレイン酸変性SEBS(製品名:タフテック(登録商標)M1911、酸価:2mgCH3ONa/g)を用いた以外は、実施例1と同様にして、各種操作、測定、及び評価を実施した。結果を表1に示す。
重合体1のシクロヘキサン溶液を調製する際に、酸価の異なる重合体1として、以下のようにして、準備した重合体1を用いた以外は、実施例1と同様にして、各種操作、測定、及び評価を実施した。結果を表1に示す。
<重合体1の準備>
セパラブルフラスコに、旭化成社製マレイン酸変性SEBS(製品名:タフテック(登録商標)M1913)100部、tert-ブチルベンゼン900部、無水マレイン酸7部、及びジクミルペルオキシド(日本油脂社製、パークミルD)2.5部を投入し、窒素雰囲気下で撹拌しながら130℃で5時間反応させた。反応終了後、反応液をメタノールに徐々に加えることにより、ポリマーを析出させた。析出させたポリマーをメタノールでさらに洗浄した。洗浄後のポリマーを60℃で1日真空乾燥させた。その後、酸価を測定したところ、15mgCH3ONa/gであった。
重合体1のシクロヘキサン溶液を調製する際に、酸価の異なる重合体1として、以下のようにして準備した重合体1を用いた以外は、実施例1と同様にして、各種操作、測定、及び評価を実施した。結果を表1に示す。
<重合体1の準備>
実施例5の無水マレイン酸量を7部から18部にしたこと以外は、実施例5と同様にしてポリマーを調製した。得られたポリマーの酸価を測定したところ、25mgCH3ONa/gであった。
重合体2のシクロヘキサン溶液を調製する際に、脂肪族共役ジエン単量体として、1,3-ブタジエン70.0kgに代えて、イソプレン70.0kgを用いたこと以外は、実施例1と同様にして、各種操作、測定、及び評価を実施した。結果を表1に示す。
重合体2として、イソプレンゴム(日本ゼオン社製、「Nipol IR2200」)を用いて、シクロヘキサンに対して溶解させて濃度5.0質量%のイソプレンゴムのシクロヘキサン溶液を調製して用いた以外は、実施例1と同様にして、各種操作、測定、及び評価を実施した。結果を表1に示す。
実施例1と同じ組成の、重合体1のシクロヘキサン溶液と、重合体2のシクロヘキサン溶液と、乳化剤水溶液とを、実施例1と同様にしてそれぞれ調製した。そして、得られた重合体1のシクロヘキサン溶液500gと乳化剤水溶液700gとをタンクに投入し、実施例1の「予備混合操作」における操作と同様の高圧乳化分散機を用いた操作を行った。そして、以降の操作も、実施例1と同様にして、重合体1を含む(重合体2は含まない)重合体粒子を含有する水分散液1を得た。別途、重合体2のシクロヘキサン溶液についても、同様の操作を実施し、重合体2を含む(重合体1は含まない)重合体粒子を含有する水分散液2を得た。そして、負極用スラリー組成物の調製にあたり、グラファイト97.5部に対して、重合体1を含む(重合体2は含まない)重合体粒子が固形分相当量で0.75部となるように水分散液1を、重合体2を含む(重合体1は含まない)重合体粒子が固形分相当量で0.75部となるように水分散液2を、それぞれ投入した。
これらの点以外は、実施例1と同様にして、各種操作、測定、及び評価を実施した。結果を表1に示す。
実施例1と同じ組成の、重合体2のシクロヘキサン溶液と、乳化剤水溶液とを、実施例1と同様にしてそれぞれ調製した。そして、得られた重合体2のシクロヘキサン溶液500gと乳化剤水溶液700gとをタンクに投入し、実施例1の「予備混合操作」における操作と同様の高圧乳化分散機を用いた操作を行った。そして、以降の操作も、実施例1と同様にして、重合体2を含む(重合体1は含まない)重合体粒子を含有する水分散液を得た。そして、負極用スラリー組成物の調製にあたり、グラファイト97.5部に対して、重合体2を含む(重合体1は含まない)重合体粒子が固形分相当量で1.5部となるように水分散液を投入した。
重合体1に関連する操作は行わず、重合体1を含む重合体粒子を含有しないスラリー組成物を得た。
これらの点以外は、実施例1と同様にして、各種操作、測定、及び評価を実施した。結果を表1に示す。
実施例1と同じ組成の、重合体1のシクロヘキサン溶液と、乳化剤水溶液とを、実施例1と同様にしてそれぞれ調製した。そして、得られた重合体1のシクロヘキサン溶液500gと乳化剤水溶液700gとをタンクに投入し、実施例1の「予備混合操作」における操作と同様の高圧乳化分散機を用いた操作を行った。そして、以降の操作も、実施例1と同様にして、重合体1を含む(重合体2は含まない)重合体粒子を含有する水分散液を得た。そして、負極用スラリー組成物の調製にあたり、グラファイト97.5部に対して、重合体1を含む(重合体2は含まない)重合体粒子が固形分相当量で1.5部となるように水分散液を投入した。
重合体2に関連する操作は行わず、重合体2を含む重合体粒子を含有しないスラリー組成物を得た。
これらの点以外は、実施例1と同様にして、各種操作、測定、及び評価を実施した。結果を表1に示す。
「M-SEBS」は、無水マレイン酸変性の(スチレン-エチレン・ブチレン-スチレン)ブロック重合体を示し、
「ST」は、スチレンを示し、
「SBS」は、(スチレン-ブタジエン-スチレン)ブロック重合体を示し、
「SIS」は、(スチレン-イソプレン-スチレン)ブロック重合体を示し
「IR」は、イソプレンゴムを示し、
「BT」は、1,3-ブタジエン単位を示し、
「IP」は、イソプレン単位を示す。
一方、重合体粒子に含まれる重合体の種類が一種であった比較例1~3では、粘度安定性に優れたスラリー組成物、及びピール強度に優れる電極の双方を提供することができなかったことが分かる。
また、本発明によれば、ピール強度に優れる非水系二次電池用電極を形成可能であり、且つ、粘度安定性に優れる非水系二次電池電極用スラリー組成物を提供することができる。
さらに、本発明によれば、ピール強度に優れる非水系二次電池用電極、及び、当該非水系二次電池用電極を備える非水系二次電池を提供することができる。
Claims (10)
- 重合体粒子を含む非水系二次電池用バインダー組成物であって、
前記重合体粒子が、酸性基含有単量体単位を有するブロック重合体である重合体1と、酸性基含有単量体単位を有さない重合体2と、を含み
前記重合体1及び重合体2の合計質量を基準として、前記重合体1の割合が10質量%以上90質量%以下であり、且つ、
前記重合体2が、脂肪族共役ジエン単量体単位及びアルキレン構造単位の少なくとも一方を含み、前記重合体2に含まれる全繰り返し単位の合計質量を基準とした場合の、前記脂肪族共役ジエン単量体単位及びアルキレン構造単位の合計割合が、55質量%以上である、
非水系二次電池用バインダー組成物。 - 前記重合体1が、芳香族ビニル単量体単位からなるブロック領域を含む主鎖と、該主鎖に対して結合したグラフト部分とを有し、
前記主鎖に含まれる全繰り返し単位の合計質量を基準として、前記芳香族ビニル単量体単位の割合が10質量%以上50質量%以下であり、且つ、
前記グラフト部分に前記酸性基含有単量体単位を含む、
請求項1に記載の非水系二次電池用バインダー組成物。 - 前記重合体1の酸価が、0.5mgCH3ONa/g以上30mgCH3ONa/g以下である、請求項1又は2に記載の非水系二次電池用バインダー組成物。
- 前記重合体2がブロック重合体である、請求項1~3の何れかに記載の非水系二次電池用バインダー組成物。
- 前記重合体1が、脂肪族共役ジエン単量体単位及びアルキレン構造単位の少なくとも一方を含む、請求項1~4の何れかに記載の非水系二次電池用バインダー組成物。
- 前記重合体1の前記酸性基含有単量体単位がカルボキシル基含有単量体単位である、請求項1~5の何れかに記載の非水系二次電池用バインダー組成物。
- 請求項1~6のいずれかに記載の非水系二次電池用バインダー組成物の製造方法であって、
前記重合体1、前記重合体2、有機溶媒、乳化剤、及び水を含む予備混合物を得る工程と、
前記予備混合物を転相乳化する転相乳化工程と、
を含む、
非水系二次電池用バインダー組成物の製造方法。 - 電極活物質と、請求項1~6のいずれかに記載の非水系二次電池用バインダー組成物とを含む、非水系二次電池電極用スラリー組成物。
- 請求項8に記載の非水系二次電池電極用スラリー組成物を用いて形成された電極合材層を備える、非水系二次電池用電極。
- 請求項9に記載の非水系二次電池用電極を備える、非水系二次電池。
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| KR1020227005637A KR20220069924A (ko) | 2019-09-30 | 2020-09-25 | 비수계 이차 전지용 바인더 조성물 및 그 제조 방법, 비수계 이차 전지 전극용 슬러리 조성물, 비수계 이차 전지용 전극, 그리고 비수계 이차 전지 |
| US17/753,833 US20220336814A1 (en) | 2019-09-30 | 2020-09-25 | Binder composition for non-aqueous secondary battery and method of producing same, slurry composition for non-aqueous secondary battery electrode, electrode for non-aqueous secondary battery, and non-aqueous secondary battery |
| EP20870985.7A EP4039743A4 (en) | 2019-09-30 | 2020-09-25 | BINDER COMPOSITION FOR NON-AQUEOUS SECONDARY BATTERY AS WELL AS ASSOCIATED MANUFACTURING METHOD, THICK SUSPENSION COMPOSITION FOR NON-AQUEOUS SECONDARY BATTERY ELECTRODE, ELECTRODE FOR NON-AQUEOUS SECONDARY BATTERY AND NON-AQUEOUS SECONDARY BATTERY |
| CN202080058460.3A CN114258601A (zh) | 2019-09-30 | 2020-09-25 | 非水系二次电池用粘结剂组合物及其制造方法、非水系二次电池电极用浆料组合物、非水系二次电池用电极、以及非水系二次电池 |
| JP2021551199A JPWO2021065742A1 (ja) | 2019-09-30 | 2020-09-25 |
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| KR20230143122A (ko) * | 2022-04-04 | 2023-10-11 | 주식회사 엘지화학 | 리튬 이차 전지용 절연층 조성물 및 이를 포함하는 리튬 이차 전지 |
| WO2023195750A1 (ko) * | 2022-04-04 | 2023-10-12 | 주식회사 엘지화학 | 리튬 이차 전지용 절연층 조성물 및 이를 포함하는 리튬 이차 전지 |
| KR20240088962A (ko) | 2021-10-29 | 2024-06-20 | 니폰 제온 가부시키가이샤 | 비수계 이차 전지 부극용 바인더 조성물, 비수계 이차 전지 부극용 슬러리 조성물, 비수계 이차 전지용 부극, 및 비수계 이차 전지 |
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| JPWO2021065742A1 (ja) | 2021-04-08 |
| EP4039743A1 (en) | 2022-08-10 |
| CN114258601A (zh) | 2022-03-29 |
| US20220336814A1 (en) | 2022-10-20 |
| EP4039743A4 (en) | 2023-10-18 |
| KR20220069924A (ko) | 2022-05-27 |
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