WO2023286833A1 - 二次電池電極用樹脂組成物、二次電池電極用合材スラリーの製造方法、電極膜の製造方法、及び二次電池の製造方法 - Google Patents
二次電池電極用樹脂組成物、二次電池電極用合材スラリーの製造方法、電極膜の製造方法、及び二次電池の製造方法 Download PDFInfo
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- WO2023286833A1 WO2023286833A1 PCT/JP2022/027695 JP2022027695W WO2023286833A1 WO 2023286833 A1 WO2023286833 A1 WO 2023286833A1 JP 2022027695 W JP2022027695 W JP 2022027695W WO 2023286833 A1 WO2023286833 A1 WO 2023286833A1
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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
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
- H01M4/621—Binders
- H01M4/622—Binders being polymers
- H01M4/623—Binders being polymers fluorinated polymers
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- 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
-
- 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
- H01M4/621—Binders
- H01M4/622—Binders being polymers
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
- H01M4/624—Electric conductive fillers
- H01M4/625—Carbon or graphite
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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 resin composition for secondary battery electrodes, a method for producing a mixture slurry for secondary battery electrodes, a method for producing an electrode film, and a method for producing a secondary battery.
- non-aqueous electrolyte secondary batteries using a non-aqueous electrolyte especially lithium ion secondary batteries, have come to be used in many devices due to their characteristics of high energy density and high voltage.
- the electrode of the secondary battery is made by coating a current collector with a mixture slurry containing a positive electrode active material or negative electrode active material, a conductive material, a binder resin, and the like.
- a conductive material dispersion is prepared by dispersing a conductive material in a dispersion medium, and an active material and a binder resin are added to the conductive material dispersion to prepare a mixture slurry, so that the conductive material is uniformly dispersed in the electrode film. It is dispersedly contained and can improve the conductivity of the electrode film.
- the conductive material dispersion can be commonly used for various mixed material slurries, but the mixed material slurry is prepared by adjusting the type of active material, the mixing ratio of each component, etc.
- the dispersibility and fluidity are maintained even while the conductive material dispersion is stored before adding the active material. Furthermore, if the resin composition in which the binder resin is added to the conductive material dispersion can be stored, the work of preparing the mixture slurry can be simplified.
- Carbon black, fullerene, graphene, fine carbon materials, etc. are used as conductive materials.
- carbon nanotubes which are a kind of fine carbon fibers, are often used.
- the conductivity of the electrode film can be improved and the electrode resistance can be reduced.
- the electrode resistance can be reduced, the load resistance of the battery can be improved, the strength of the electrode can be increased, and the expansion and contraction properties of the electrode can be increased. Cycle life can be improved.
- multi-walled carbon nanotubes with an outer diameter of several nanometers to several tens of nanometers are relatively inexpensive and are being put to practical use.
- Patent Document 1 discloses a conductive material containing bundled carbon nanotubes, a dispersant such as a hydrogenated nitrile-butadiene rubber, and a dispersion medium. Disclosed is a conductive material dispersion that is 18°.
- a composition obtained by adding an active material and a binder to a conductive material dispersion containing carbon nanotubes has a reduced viscosity and elasticity, changes rapidly during coating, and causes cracks in the formation of an electrode active material layer. Therefore, the phase angle of the conductive material dispersion is controlled to 18° or less to provide solid-like properties, thereby preventing cracks from occurring in the produced electrode active material layer.
- Patent document 2 contains a conductive material containing bundled carbon nanotubes, a dispersant containing hydrogenated nitrile rubber, and a dispersion medium, and when measured with a rheometer, the complex elastic modulus at a frequency of 1 Hz (G *
- a conductive material paste 1 is obtained by mixing a conductive material such as acetylene black and a first binder, a second binder is added to the conductive material paste 1 to obtain a conductive material paste 2, and a conductive A method for producing a secondary battery positive electrode slurry by mixing a positive electrode active material with a material paste 2 is disclosed.
- the first binder contains at least one monomer selected from the group consisting of conjugated diene monomer units, 1-olefin monomer units, and (meth)acrylic acid ester monomer units.
- the conductive material is formed in the resulting slurry by adding and mixing the first binder and the second binder in this order, including a resin containing a body unit, the second binder including a fluorine-based polymer such as polyvinylidene fluoride. It is appropriately dispersed, and a good conductive network is formed between the conductive materials in the positive electrode mixture layer to be produced, thereby improving the cycle characteristics of the secondary battery and suppressing capacity deterioration at low temperatures.
- Patent Document 4 a conductive material paste containing a conductive material such as acetylene black, a binder, and a fluorine-based polymer such as polyvinylidene fluoride and having a solid content concentration of 5% by mass or more and 15% by mass or less is prepared.
- a method for producing a secondary battery positive electrode slurry by mixing a material paste and a positive electrode active material is disclosed. According to Patent Document 4, when the solid content of the conductive material paste is within this range, a good conductive network is formed between the conductive materials in the positive electrode mixture layer to be produced, and the cycle characteristics of the secondary battery are improved. , the internal resistance is reduced.
- the finer the conductive material the more efficient the conductive network can be formed. becomes difficult. If the concentration of the conductive material is forcibly increased, the viscosity of the resin composition increases and the fluidity deteriorates. In addition, the fine conductive material and the binder resin may get entangled and cause poor dispersion. A resin composition with poor fluidity may cause a problem that it becomes difficult to remove the resin composition from a tank or the like when the resin composition is transported in a tank or the like or stored for a long period of time. On the other hand, a resin composition with a low conductive material concentration poses problems such as a low degree of freedom in design when a material such as an active material is blended, and a high transportation cost per solid content of the conductive material. Therefore, it is an urgent need to obtain a resin composition in which fine conductive materials are well dispersed in a state of high fluidity.
- the conductive material dispersion disclosed in Patent Document 1 has relatively strong solid-like properties, and the conductive material dispersion disclosed in Patent Document 2 has relatively strong elastic behavior. There is a problem that it is unsuitable for storage of In Patent Document 1, a conductive material dispersion having high solid-like characteristics is obtained by controlling the phase angle, and then an active material and a binder are added to prepare a composition. However, conductive material dispersions with high solid-like properties can be highly viscous and less miscible with subsequently added binders. In Patent Document 2, a conductive material dispersion liquid in which dispersibility and viscosity characteristics are controlled by a complex elastic modulus is obtained, and then an active material and a binder are added to prepare a composition.
- simply controlling the complex elastic modulus of the conductive material dispersion may not provide sufficient miscibility with the subsequently added binder.
- a binder resin is added to a carbon nanotube dispersion liquid finely dispersed while maintaining the fiber length of the carbon nanotubes, the carbon nanotubes aggregate or the binder resin gels, resulting in dispersibility and fluidity of the resin composition. It may reduce sexuality.
- Patent Documents 3 and 4 acetylene black is specifically studied as a conductive material, but carbon nanotubes are not sufficiently studied.
- fibrous carbon materials such as carbon nanotubes
- the fibers are broken by dispersion treatment or stirring treatment in the manufacturing process of the mixture slurry, the conductive network between the conductive materials in the electrode film may deteriorate.
- the fibers and the resin component are likely to be entangled and aggregated, and if the electrode film is produced in a state where the fibers are not unraveled, the conductive material in the electrode film may be reduced. The conductive network between them can be degraded.
- the inventors of the present invention conducted a detailed comparative study on fine differences in the dispersion state of the conductive material, and found that when fibrous carbon nanotubes are used as the conductive material, the particle size distribution, which has often been used as an index of the degree of dispersion, is It was found that even with the same measurement value, the characteristics of the viscosities when used in secondary batteries may differ, and it was found that the dispersion state of the conductive material was not accurately captured. For example, in the case of the particle size distribution, since fibrous non-spherical particles are calculated assuming that they are spherical, deviation from the actual situation is likely to occur.
- the problem to be solved by the present invention is to finely control the dispersed state of carbon nanotubes, which is a conductive material, and to provide a resin composition for secondary battery electrodes that has high dispersibility and fluidity in a state containing a fluororesin, and
- An object of the present invention is to provide a mixture slurry for a secondary battery electrode in which carbon nanotubes are well dispersed while containing an active material. More specifically, the object is to provide a non-aqueous electrolyte secondary battery with high output, high capacity and long life, and an electrode film used therein.
- a conductive network can be formed in the electrode film by dispersing long fibers of the carbon nanotubes in the resin composition while maintaining them appropriately without breaking them, and forming an electrode film using this resin composition. I found This makes it possible to provide a secondary battery with high output, high capacity, and long life.
- the present invention includes the following embodiments. Embodiments of the present invention are not limited to the following.
- ⁇ 1> Contains a carbon nanotube, a dispersant, a fluororesin, and a dispersion medium, does not contain an active material, and is a complex elastic modulus X (Pa) and a phase angle Y at 25 ° C. and 1 Hz by dynamic viscoelasticity measurement
- the resin composition for a secondary battery electrode according to ⁇ 1> which has a complex elastic modulus of 0.1 Pa or more and 300 Pa or less at 25°C and 1 Hz by dynamic viscoelasticity measurement.
- ⁇ 3> The resin composition for a secondary battery electrode according to ⁇ 1> or ⁇ 2>, which has a phase angle of 3° or more and 90° or less at 25° C. and 1 Hz by dynamic viscoelasticity measurement.
- ⁇ 4> The secondary battery electrode according to any one of ⁇ 1> to ⁇ 3>, wherein the content of the carbon nanotubes is 0.5% by mass or more and 15% by mass or less with respect to the total amount of the resin composition.
- Resin composition. ⁇ 5> The resin composition for a secondary battery electrode according to any one of ⁇ 1> to ⁇ 4>, wherein the mass ratio of the dispersant to the carbon nanotubes is 0.01 or more and 2 or less.
- ⁇ 6> The resin composition for a secondary battery electrode according to any one of ⁇ 1> to ⁇ 5>, wherein the mass ratio of the fluororesin to the carbon nanotubes is 0.1 or more and 10 or less.
- ⁇ 7> The resin composition for a secondary battery electrode according to any one of ⁇ 1> to ⁇ 6>, wherein the carbon nanotubes include single-walled carbon nanotubes and multi-walled carbon nanotubes.
- ⁇ 8> The resin composition for a secondary battery electrode according to any one of ⁇ 1> to ⁇ 7>, further containing carbon black.
- a method for producing a mixture slurry for a secondary battery electrode comprising adding an active material to the resin composition for a secondary battery electrode according to any one of ⁇ 1> to ⁇ 8>.
- a method for producing a mixture slurry comprising adding an active material to the resin composition for a secondary battery electrode according to any one of ⁇ 1> to ⁇ 8>.
- An active material is added to the resin composition for a secondary battery electrode according to any one of ⁇ 1> to ⁇ 8> to prepare a mixture slurry, and the mixture slurry is applied to form an electrode film.
- a method of manufacturing an electrode film comprising: ⁇ 12> A method for producing a secondary battery containing a positive electrode, a negative electrode, and an electrolyte, wherein an active material is added to the resin composition for a secondary battery electrode according to any one of ⁇ 1> to ⁇ 8>.
- a method for manufacturing a secondary battery comprising: preparing a material slurry; and forming at least one of the positive electrode and the negative electrode by applying the mixture slurry to a current collector to form an electrode film.
- a resin composition for secondary battery electrodes having high fluidity and dispersibility.
- a secondary battery electrode mixture slurry in which carbon nanotubes are well dispersed it is possible to provide a non-aqueous electrolyte secondary battery with high output, high capacity, and long life, and an electrode film used therein.
- the resin composition for a secondary battery electrode the method for producing a mixture slurry for a secondary battery electrode, the method for producing an electrode film, and the method for producing a secondary battery, which are embodiments of the present invention, will be described in detail.
- the present invention is not limited to the following embodiments, and the present invention also includes embodiments carried out without changing the gist of the invention.
- carbon nanotubes are sometimes referred to as “CNT”.
- Hydrogenated nitrile rubber is sometimes abbreviated as “H-NBR” and N-methyl-2-pyrrolidone as “NMP”.
- the carbon nanotube dispersion may be simply referred to as “CNT dispersion” or “dispersion”
- resin composition for secondary battery electrodes may be simply referred to as “resin composition”.
- the resin composition for secondary battery electrodes contains carbon nanotubes, a dispersant, a fluororesin, and a dispersion medium, and may further contain optional components.
- Carbon nanotubes (CNTs) function as conductive materials.
- the resin composition may contain a conductive material other than carbon nanotubes. Examples of other conductive materials include carbon materials such as carbon black, fullerene, graphene, multilayer graphene, and graphite.
- carbon black is preferable from the viewpoint of adsorption performance of the dispersant, and examples thereof include carbon black such as acetylene black, furnace black, hollow carbon black, and ketjen black. These carbon blacks may be neutral, acidic or basic, and oxidized carbon black or graphitized carbon black may be used.
- Other conductive materials may be used singly or in combination of two or more.
- the CNTs to be added to the resin composition preferably have the following physical properties.
- the CNT has a shape in which planar graphite is rolled into a cylindrical shape, and includes single-wall CNT and multi-wall CNT, and these may be mixed.
- Single-walled CNTs have a structure in which a single layer of graphite is wound.
- Multilayer CNTs have a structure in which two or more layers of graphite are wound.
- the side wall of the CNT may not have a graphite structure.
- CNTs with sidewalls having, for example, an amorphous structure are also CNTs herein.
- the shape of CNT is not limited. Such shapes include a variety of shapes including needles, cylindrical tubes, fish bones (fish bones or cup stacks), tramp (platelets) and coils. Among others, the shape of the CNT is preferably needle-like or cylindrical tube-like. CNTs may be of a single shape or a combination of two or more shapes.
- CNTs include, for example, graphite whiskers, filamentous carbon, graphite fibers, ultrafine carbon tubes, carbon tubes, carbon fibrils, carbon microtubes, and carbon nanofibers.
- Carbon nanotubes may have a single form or a form in which two or more of these forms are combined.
- the average outer diameter of CNTs is preferably 1 nm or more, more preferably 3 nm or more. Also, it is preferably 30 nm or less, more preferably 20 nm or less, and even more preferably 15 nm or less.
- the average outer diameter of CNTs can be calculated by first observing and imaging the CNTs with a transmission electron microscope, selecting arbitrary 300 CNTs in the observation photograph, and measuring the outer diameters of each.
- the resin composition may be prepared by separately preparing two or more types of CNTs having different average outer diameters and adding them to the dispersion medium.
- the average outer diameter of the first CNTs is preferably 1 nm or more and less than 5 nm.
- the average outer diameter of the second CNTs is preferably 3 nm or more and 30 nm or less, more preferably 5 nm or more and 30 nm or less, and even more preferably 20 nm or less.
- the mass ratio of the first CNTs and the second CNTs is preferably 1:1 to 1:100, and 1:3 to 1:1:1. 100 is more preferred, 1:10 to 1:100 is more preferred, and 1:10 to 1:50 is even more preferred.
- the average outer diameter of the single-walled carbon nanotube is preferably 1 nm or more and 3 nm or less, and 1.3 nm or more. It is more preferably 2.5 nm or less, and even more preferably 1.5 nm or more and 2.0 nm or less.
- the average outer diameter of the multi-walled carbon nanotubes is preferably more than 3 nm and 30 nm or less, more preferably 3 nm or more and 20 nm or less, and even more preferably 5 nm or more and 15 nm or less.
- a combination of single-walled carbon nanotubes and multi-walled carbon nanotubes may be included as carbon nanotubes.
- the mass ratio of single-walled carbon nanotubes and multi-walled carbon nanotubes is preferably 1:1 to 1:100, more preferably 1:2 to 1:50, and 1:3 to 1:1:1. 10 is more preferred. Since single-walled carbon nanotubes and multi-walled carbon nanotubes have different outer diameters and fiber lengths, they are different in terms of good conductive network formation and dispersion stabilization. By setting the mass ratio of the single-walled carbon nanotubes to the multi-walled carbon nanotubes within the above range, the entanglement of the carbon nanotubes is suppressed, and a dispersion having excellent fluidity can be obtained.
- the average fiber length of CNTs is preferably 0.5 ⁇ m or longer, more preferably 0.8 ⁇ m or longer, and even more preferably 1.0 ⁇ m or longer. Moreover, it is preferably 20 ⁇ m or less, more preferably 10 ⁇ m or less.
- the average fiber length of CNTs can be calculated by first observing and photographing CNTs with a scanning electron microscope, selecting arbitrary 300 CNTs in the observation photograph, and measuring the fiber length of each.
- the aspect ratio is the value obtained by dividing the CNT fiber length by the outer diameter. Using the average fiber length and average outer diameter values, a representative aspect ratio can be determined. A conductive material having a higher aspect ratio can provide a higher conductivity when an electrode is formed.
- the aspect ratio of CNTs is preferably 30 or more, more preferably 50 or more, and even more preferably 80 or more. Also, it is preferably 10,000 or less, more preferably 3,000 or less, and even more preferably 1,000 or less.
- the specific surface area of CNTs is preferably 100 m 2 /g or more, more preferably 150 m 2 /g or more, and even more preferably 200 m 2 /g or more. Also, it is preferably 1200 m 2 /g or less, more preferably 1000 m 2 /g or less.
- the specific surface area of CNT is calculated by the BET method based on nitrogen adsorption measurement. When the average outer diameter, average fiber length, aspect ratio, and specific surface area of the CNT are within the above ranges, it becomes easier to form a well-developed conductive path in the electrode.
- the carbon purity of CNT is expressed by the content of carbon atoms (% by mass) in the CNT.
- the carbon purity is preferably 80% by mass or more, more preferably 90% by mass or more, still more preferably 95% by mass or more, and 98% by mass or more with respect to 100% by mass of CNT. Especially preferred.
- CNTs that have undergone a high-purification treatment may be used.
- the method of purification treatment is not particularly limited, and a known method can be used.
- a method of evaporating impurities by treating at a high temperature (for example, 3000° C.) under an inert atmosphere may be used. This method is preferable in that it can be treated under conditions with relatively little risk of explosion or the like.
- a method may be used in which a halogen-containing gas (chlorine gas, fluorine gas, carbon tetrachloride gas, carbon tetrafluoride gas, etc.) is mixed with an inert gas and heat-treated to evaporate halogenated impurities. Since the boiling point of impurities is lowered by halogenation, they can be removed at a lower temperature (e.g., 1600°C) compared to the case without halogenation, without changing physical properties such as crystallinity, density, and conductivity of CNTs. It is preferable in that the carbon purity can be increased.
- a halogen-containing gas chlorine gas, fluorine gas, carbon tetrachloride gas, carbon tetrafluoride gas, etc.
- the CNTs are densified and then heat-treated, it is possible to suppress scattering of the CNTs and to increase the amount of treatment, thereby efficiently purifying the CNTs.
- a method of impregnating CNTs in an acidic or basic solution and dissolving and removing impurities may be used.
- functional groups may be introduced to the surface or end of CNTs, and a small amount of functional groups tends to improve dispersibility.
- the functional group is large, the electrical conductivity tends to be lowered in some cases.
- the CNTs When dispersing CNTs in a disperser by collision with media such as a bead mill, or when performing a treatment that repeatedly passes the disperser over a long period of time, the CNTs may break and produce short pieces of carbonaceous matter. .
- the short piece-like carbonaceous matter When the short piece-like carbonaceous matter is generated, the viscosity of the resin composition decreases, and the gloss of the coating film obtained by coating and drying the resin composition increases. seems good.
- the short piece-like carbonaceous material has high contact resistance and is difficult to form a conductive network. Therefore, the resin composition produced through such a dispersion treatment may deteriorate the resistance of the electrode.
- the extent to which short flakes of carbon are produced can be confirmed by diluting the dispersion liquid, dropping it onto a base material with a smooth surface and good affinity for the dispersion medium, and then drying the sample by observing it with a scanning electron microscope. can.
- An electrode with high conductivity can be obtained by adjusting the dispersion conditions and the composition of the dispersion liquid so that carbonaceous matter of 0.1 ⁇ m or less does not occur.
- Carbon nanotubes may be surface-treated carbon nanotubes.
- the carbon nanotube may be a carbon nanotube derivative provided with a functional group typified by a carboxyl group.
- a carbon nanotube encapsulating a substance typified by an organic compound, a metal atom, or fullerene can also be used.
- Carbon nanotubes can be carbon nanotubes manufactured by any method. Carbon nanotubes can generally be produced by, but not limited to, laser ablation, arc discharge, thermal CVD, plasma CVD, and combustion methods. For example, carbon nanotubes can be produced by contact-reacting a carbon source with a catalyst at 500 to 1000° C. in an atmosphere with an oxygen concentration of 1% by volume or less. The carbon source may be at least one of hydrocarbons and alcohols.
- any conventionally known raw material gas can be used as a carbon source for carbon nanotubes.
- a raw material gas containing carbon hydrocarbons represented by methane, ethylene, propane, butane and acetylene, carbon monoxide, and alcohols can be used, but not limited thereto.
- hydrocarbons represented by methane, ethylene, propane, butane and acetylene, carbon monoxide, and alcohols can be used, but not limited thereto.
- (meth)acrylic polymers polymers derived from ethylenically unsaturated hydrocarbons, cellulose derivatives, copolymers thereof, and the like can be used.
- polymers derived from ethylenically unsaturated hydrocarbons include polyvinyl alcohol-based resins, polyvinylpyrrolidone-based resins, polyacrylonitrile-based resins, and nitrile rubbers.
- Polyvinyl alcohol-based resins include polyvinyl alcohol, modified polyvinyl alcohol having functional groups other than hydroxyl groups (e.g., acetyl group, sulfo group, carboxy group, carbonyl group, amino group), polyvinyl alcohol modified with various salts, and other anions.
- polyvinyl alcohol polyvinyl acetal (polyvinyl acetoacetal, polyvinyl butyral, etc.) acetal-modified (acetoacetal-modified or butyral-modified, etc.) with aldehydes, and the like can be mentioned.
- the polyacrylonitrile-based resin may be a homopolymer of polyacrylonitrile, a copolymer of polyacrylonitrile, a modified product thereof, or the like.
- the polyacrylonitrile-based resin may be a homopolymer of polyacrylonitrile, a copolymer of polyacrylonitrile, a modified product thereof, or the like.
- a polyacrylonitrile-based resin or the like having at least one selected from the group consisting of a hydrogen group, a basic group, an alkyl group introduced from a (meth)acrylic acid alkyl ester, etc. is preferable, for example, JP-A-2020- An acrylonitrile copolymer described in No. 163362 can be used.
- nitrile rubbers include acrylonitrile-butadiene rubber and hydrogenated acrylonitrile-butadiene rubber.
- Cellulose derivatives include cellulose acetate, cellulose acetate butyrate, cellulose butyrate, cyanoethyl cellulose, ethylhydroxyethyl cellulose, nitrocellulose, methyl cellulose, ethyl cellulose, hydroxyethyl cellulose, hydroxypropyl cellulose, hydroxypropyl methyl cellulose, carboxymethyl cellulose, etc., or these copolymers, and the like.
- WO 2008/108360 pamphlet JP 2018-192379, JP 2019-087304, JP 6524479, JP 2009-026744 may be used dispersants described in, but these is not limited to Particularly preferred are methyl cellulose, ethyl cellulose, polyvinyl alcohol, polyvinyl butyral, polyvinylpyrrolidone, polyacrylonitrile homopolymers, polyacrylonitrile copolymers, and hydrogenated acrylonitrile-butadiene rubber. Polymers obtained by introducing other substituents into some of these polymers, modified polymers, and the like may also be used.
- the weight-average molecular weight of the resin-type dispersant is preferably 500,000 or less, and preferably 300,000 or less, from the viewpoint of the affinity balance between the substance to be dispersed and the dispersion medium and the resistance to the electrolytic solution. is more preferably 3,000 or more, and more preferably 5,000 or more.
- the resin-type dispersant may be used singly or in combination of two or more.
- polyvinyl alcohol resins examples include Kuraray Poval (polyvinyl alcohol resin manufactured by Kuraray), Gohsenol, Gohsenex (polyvinyl alcohol resin manufactured by Nippon Synthetic Chemical Industry), Denka Poval (polyvinyl alcohol resin manufactured by Denka), J-Poval ( Various grades are available under trade names such as "polyvinyl alcohol resin manufactured by Japan Vinyl Acetate & Poval Co., Ltd.”. Modified polyvinyl alcohols having various functional groups are also available. Moreover, you may use what was synthesize
- polyvinylpyrrolidone-based resins include Luvitec K17 (K value: 15.0 to 19.0, low molecular weight), K30 (K value: 27.0 to 33.0), K80 ( K value 74.0-82.0), K85 (K value 84.0-88.0), K90 (K value 88.0-92.0), K90HM (K value 92.0-96.0, high Molecular weight) (manufactured by BASF Japan), K15, K30, K90, K120 (manufactured by ISP), polyvinylpyrrolidone K30 (K value 27.0 to 33.0), K85 (K value 84.0 to 88.0), K90 ( K value 88.0-96.0) (manufactured by Nippon Shokubai), PVP K12 (K value 10-14), K15 (K value 13-19), K30 (K26-K35), K60 (K value 50-62) , K90 (K value 88 to 100), K120 (K value 114 to 130) (manufactured by DSP Go
- the K value of polyvinylpyrrolidone is preferably 150 or less, more preferably 100 or less, and even more preferably 85 or less, from the viewpoint of preventing viscosity increase.
- nitrile rubbers include Therban (hydrogenated nitrile rubber manufactured by Aranseo), Baymod (nitrile rubber manufactured by Aranseo), Zetpole (hydrogenated nitrile rubber manufactured by Nippon Zeon), Nipole NBR (manufactured by Nippon Zeon Nitrile rubber) and other trade names are available in various grades with different nitrile ratios, hydrogenation rates, molecular weights, and the like. Moreover, you may use what was synthesize
- a surfactant may be used in place of or in addition to the resin-type dispersant described above.
- Surfactants are classified into anionic, cationic, amphoteric ionic surfactants, and nonionic surfactants.
- a polymer containing at least an aliphatic hydrocarbon structural unit and a nitrile group-containing structural unit may be used as the resin-type dispersant.
- the aliphatic hydrocarbon structural units of the polymer may include alkylene structural units. This polymer may be hydrogenated.
- the aliphatic hydrocarbon structural unit is a structural unit containing an aliphatic hydrocarbon structure, preferably a structural unit consisting only of an aliphatic hydrocarbon structure.
- the aliphatic hydrocarbon structure includes at least a saturated aliphatic hydrocarbon structure and may further include an unsaturated aliphatic hydrocarbon structure.
- the aliphatic hydrocarbon structure preferably includes at least a linear aliphatic hydrocarbon structure, and may further include a branched aliphatic hydrocarbon structure.
- Examples of aliphatic hydrocarbon structural units include alkylene structural units, alkenylene structural units, alkyl structural units, alkanetriyl structural units, and alkanetetrayl structural units.
- a structural unit containing a branch point such as an alkanetriyl structural unit or an alkanetetrayl structural unit is a structural unit different from a structural unit containing a branched alkylene structure and a structural unit containing a branched alkyl structure, which will be described later.
- the aliphatic hydrocarbon structural unit preferably contains at least an alkylene structural unit.
- the alkylene structural unit is a structural unit containing an alkylene structure, preferably a structural unit consisting of only an alkylene structure.
- the alkylene structure is preferably a linear alkylene structure or a branched alkylene structure.
- the alkylene structural unit preferably contains a structural unit represented by the following general formula (1B).
- the alkylene structural unit preferably contains a structural unit represented by the following general formula (1C).
- n represents an integer of 1 or more.
- n is preferably an integer of 4 or less, more preferably an integer of 3 or less, and even more preferably an integer of 2 or less.
- n is preferably two.
- a polymer is prepared by a polymerization reaction using a monomer composition containing an ⁇ -olefin monomer.
- the polymer prepared contains ⁇ -olefin monomeric units.
- the final polymer contains ⁇ -olefin monomer units as alkylene structural units.
- the number of carbon atoms in the conjugated diene monomer is 4 or more, preferably 4 or more and 6 or less.
- conjugated diene monomers include conjugated diene compounds such as 1,3-butadiene, isoprene, 2,3-dimethyl-1,3-butadiene, and 1,3-pentadiene. Among them, 1,3-butadiene is preferred.
- the alkylene structural unit preferably contains a structural unit obtained by hydrogenating a conjugated diene monomer unit (hydrogenated conjugated diene monomer unit), and is obtained by hydrogenating a 1,3-butadiene monomer unit. More preferably, it contains structural units (hydrogenated 1,3-butadiene monomer units).
- a conjugated diene monomer can be used individually by 1 type or in combination of 2 or more types.
- the hydrogenation is preferably a method that can selectively hydrogenate conjugated diene monomer units.
- Examples of the hydrogenation method include known methods such as an oil layer hydrogenation method and a water layer hydrogenation method.
- the number of carbon atoms in the ⁇ -olefin monomer is 2 or more, preferably 3 or more, more preferably 4 or more.
- the number of carbon atoms in the ⁇ -olefin monomer is preferably 6 or less, more preferably 5 or less.
- Examples of ⁇ -olefin monomers include ⁇ -olefin compounds such as ethylene, propylene, 1-butene and 1-hexene. The ⁇ -olefin monomers can be used singly or in combination of two or more.
- the alkylene structural unit may include a structural unit containing a linear alkylene structure and a structural unit containing a branched alkylene structure.
- the content of the branched alkylene structure is based on the mass of the alkylene structural unit (i.e., alkylene When the mass of the structural unit is 100% by mass), it is preferably 70% by mass or less, more preferably 65% by mass or less. In particular, it is preferably 20% by mass or less, more preferably 18% by mass or less, and even more preferably 15% by mass or less.
- the content of the alkylene structural unit is based on the total mass of the aliphatic hydrocarbon structural unit (that is, when the mass of the aliphatic hydrocarbon structural unit is 100% by mass), It is preferably 60% by mass or more, more preferably 70% by mass or more, still more preferably 80% by mass or more, and particularly preferably 90% by mass or more.
- the content of the alkylene structural unit is, for example, less than 100% by mass based on the total mass of the aliphatic hydrocarbon structural units (that is, when the mass of the aliphatic hydrocarbon structural units is 100% by mass). , 99.5% by mass or less, 99% by mass or less, or 98% by mass or less.
- the content of the alkylene structural unit may be 100% by mass.
- the content of the aliphatic hydrocarbon structural unit is preferably 40% by mass or more, preferably 50% by mass or more, based on the mass of the polymer (that is, when the mass of the polymer is 100% by mass). It is more preferable that the content is 60% by mass or more.
- the content of the aliphatic hydrocarbon structural unit is preferably less than 85% by mass, and not more than 75% by mass, based on the mass of the polymer (that is, when the mass of the polymer is 100% by mass). It is more preferable that the content is 70% by mass or less.
- the nitrile group-containing structural unit is a structural unit containing a nitrile group, preferably a structural unit containing an alkylene structure substituted with a nitrile group, more preferably a structural unit consisting only of an alkylene structure substituted with a nitrile group.
- the alkylene structure is preferably a linear or branched alkylene structure.
- the nitrile group-containing structural unit may further include a structural unit containing (or consisting only of) an alkyl structure substituted with a nitrile group.
- the number of nitrile groups contained in the nitrile group-containing structural unit is preferably one.
- n represents an integer of 2 or more.
- n is preferably an integer of 6 or less, more preferably an integer of 4 or less, and even more preferably an integer of 3 or less.
- n is preferably two.
- R represents a hydrogen atom or a methyl group.
- R is preferably a hydrogen atom.
- the method for introducing the nitrile group-containing structural unit into the polymer is not particularly limited, but a method of preparing a polymer by polymerization reaction using a monomer composition containing a nitrile group-containing monomer ( method) can be preferably used.
- the finally obtained polymer contains nitrile group-containing monomer units as nitrile group-containing structural units.
- nitrile group-containing monomers capable of forming nitrile group-containing structural units include monomers containing a polymerizable carbon-carbon double bond and a nitrile group. Examples include ⁇ , ⁇ -ethylenically unsaturated group-containing compounds having a nitrile group, and specific examples include acrylonitrile and methacrylonitrile.
- the nitrile group-containing monomer preferably contains acrylonitrile from the viewpoint of increasing the intermolecular force between the polymers and/or between the polymer and the substance to be dispersed (the substance to be adsorbed).
- the nitrile group-containing monomers may be used singly or in combination of two or more.
- the content of the nitrile group-containing structural unit is preferably 15% by mass or more, and 20% by mass or more, based on the mass of the polymer (that is, when the mass of the polymer is 100% by mass). is more preferable, and 30% by mass or more is even more preferable.
- the content of the nitrile group-containing structural unit is preferably 50% by mass or less, and 46% by mass or less, based on the mass of the polymer (that is, when the mass of the polymer is 100% by mass). is more preferably 40% by mass or less.
- the adsorption to the substance to be dispersed and the affinity to the dispersion medium can be controlled, and the substance to be dispersed can be stably present in the dispersion medium. can be done.
- the affinity of the polymer to the electrolytic solution can be controlled, and problems such as an increase in the resistance of the electrolytic solution caused by the polymer dissolving in the electrolytic solution in the battery can be prevented.
- the polymer may contain any structural unit.
- optional structural units include amide group-containing structural units and carboxy group-containing structural units.
- the total content of aliphatic hydrocarbon structural units and nitrile group-containing structural units contained in the polymer is 80% by mass or more and 100% by mass or less based on the mass of the polymer. is mentioned.
- the total content is preferably 90% by mass or more, more preferably 95% by mass or more, and still more preferably 98% by mass or more.
- the content of structural units can be determined using the amount of monomer used, NMR (nuclear magnetic resonance) and/or IR (infrared spectroscopy) measurement.
- the method for adjusting the Mooney viscosity of the polymer is not particularly limited.
- the Mooney viscosity can be adjusted by changing the amount of the molecular weight modifier, etc.).
- the Mooney viscosity of the polymer can be adjusted by the following method.
- the Mooney viscosity is lowered by increasing the amount of the molecular weight modifier used in the preparation of the polymer.
- the Mooney viscosity of the polymer is lowered by modifying the nitrile group contained in the nitrile group-containing structural unit of the polymer by hydrolyzing it with a base.
- method (2c) the Mooney viscosity is lowered by applying a mechanical shearing force to the polymer.
- a method of adding a base dispersion in which a base is dispersed in a solvent to a polymer solution in which a polymer is dissolved in a solvent while stirring is preferable.
- a disper (dispersing machine), a homogenizer, or the like can be used for stirring.
- a solvent the solvent mentioned later can be used.
- the inclusion of a base in the resin composition is preferable because it enhances the wettability of CNTs in the dispersion medium, improves the dispersibility, and improves the dispersion stability.
- At least one selected from the group consisting of inorganic bases, inorganic metal salts, organic bases and organic metal salts can be used as the base to be added.
- Inorganic bases and inorganic metal salts include, for example, alkali metal or alkaline earth metal chlorides, hydroxides, carbonates, nitrates, sulfates, phosphates, tungstates, vanadates, molybdates , niobates, borates; and ammonium hydroxide.
- hydroxides or alkoxides of alkali metals or alkaline earth metals are preferable from the viewpoint of easily supplying cations.
- alkali metal hydroxides include lithium hydroxide, sodium hydroxide, potassium hydroxide and the like.
- Examples of hydroxides of alkaline earth metals include calcium hydroxide and magnesium hydroxide. Among these, it is more preferable to use at least one selected from the group consisting of lithium hydroxide, sodium hydroxide, and potassium hydroxide.
- the metal contained in the inorganic base may be a transition metal.
- organic bases include primary, secondary, and tertiary amine compounds (alkylamines, aminoalcohols, etc.) having 1 to 40 carbon atoms that may have a substituent, or organic hydroxides.
- optionally substituted primary alkylamines having 1 to 40 carbon atoms include alkylamines such as propylamine, butylamine, isobutylamine, octylamine, 2-ethylhexylamine, laurylamine, stearylamine and oleylamine; -aminoalcohols such as aminoethanol and 3-aminopropanol; 3-ethoxypropylamine, 3-lauryloxypropylamine and the like.
- Secondary alkylamines having 1 to 40 carbon atoms which may have a substituent include alkylamines such as dibutylamine, diisobutylamine, N-methylhexylamine, dioctylamine and distearylamine, and 2-methylaminoethanol. and the like.
- Optionally substituted tertiary alkylamines having 1 to 40 carbon atoms include triethylamine, tributylamine, N,N-dimethylbutylamine, N,N-diisopropylethylamine, dimethyloctylamine, trioctylamine and dimethyldecyl.
- Amines, alkylamines such as dimethyllaurylamine, dimethylmyristylamine, dimethylpalmitylamine, dimethylstearylamine and dilaurylmonomethylamine, triethanolamine, 2-(dimethylamino)ethanol and the like.
- An organic hydroxide is a salt containing an organic cation and a hydroxide ion.
- organic hydroxides include trimethyl-2-hydroxyethylammonium hydroxide, tetramethylammonium hydroxide, cetyltrimethylammonium hydroxide, hexadecyltrimethylammonium hydroxide, trimethylphenylammonium hydroxide, 3-trifluoromethyl- phenyltrimethylammonium hydroxide, benzyltrimethylammonium hydroxide and the like.
- Examples of organic metal salts include alkali metal alkoxides and alkali metal acetates.
- alkali metal alkoxides include lithium methoxide, lithium ethoxide, lithium propoxide, lithium-t-butoxide, lithium-n-butoxide, sodium methoxide, sodium ethoxide, sodium propoxide and sodium-t-butoxide.
- sodium-t-butoxide is preferable from the viewpoint of easily supplying cations.
- the metal contained in the inorganic base may be a transition metal.
- the amount of base used is preferably 0.1% by mass or more, more preferably 0.5% by mass or more, based on the mass of the polymer.
- the amount of the base used is preferably 20% by mass or less, more preferably 15% by mass or less, and even more preferably 10% by mass or less, based on the mass of the polymer. If the amount used is too small, the Mooney viscosity tends to be less likely to decrease. Using too much can cause corrosion within the dispersing device and/or the battery.
- the above method (2c) may be adjusted by applying a mechanical shear force when preparing a polymer containing a nitrile group-containing monomer unit and an aliphatic hydrocarbon structural unit, and , A polymer containing a nitrile group-containing monomer unit and an aliphatic hydrocarbon structural unit that has already been prepared may be dissolved in a soluble solvent and then subjected to a mechanical shearing force for adjustment. .
- the Mooney viscosity can also be reduced by applying a mechanical shearing force to the polymer before dissolution using a roll or kneader. It is more preferable to apply the shear force in the polymer solution state because it is efficient to use.
- the resin composition may further contain an inorganic base, an inorganic metal salt, an organic base, an organic metal salt, or a combination thereof in addition to the dispersant described above. Specifically, it may contain an inorganic base, an inorganic metal salt, an organic base, an organic metal salt, or a combination thereof described in the method (2b) for the polymer described above.
- the total amount of these is preferably 0.001 to 0.1% by mass, more preferably 0.005 to 0.05% by mass, relative to the total amount of the resin composition.
- Fluororesins include homopolymers such as polytetrafluoroethylene (PTFE), polyvinyl fluoride (PVF), polyvinylidene fluoride (PVdF), and polychlorotrifluoroethylene (PCTFE); Copolymers such as fluoroethylene propene copolymer (FEP), ethylene-tetrafluoroethylene copolymer (ETFE), ethylene-chlorotrifluoroethylene copolymer (ECTFE), tetrafluoroethylene-perfluorodioxysole copolymer (TPE/PDD), and the like. be done. You may use these individually by 1 type or in combination of 2 or more types.
- PTFE polytetrafluoroethylene
- PVdF polyvinylidene fluoride
- PCTFE polychlorotrifluoroethylene
- FEP fluoroethylene propene copolymer
- ETFE ethylene-tetrafluoroethylene copolymer
- ECTFE
- fluororesins polytetrafluoroethylene (PTFE), polyvinyl fluoride (PVF), polyvinylidene fluoride (PVdF), resins having these structural units, modified products thereof, or combinations thereof are preferable from the viewpoint of durability.
- polyvinylidene fluoride-based resins are preferable, and examples thereof include homopolymers of polyvinylidene fluoride; copolymers of vinylidene fluoride and hexafluoropropylene, tetrafluoroethylene, and the like.
- the polyvinylidene fluoride resin may be modified, for example, an acidic group such as a carboxyl group may be introduced.
- the fluororesin may be used singly or in combination of two or more.
- the weight average molecular weight (Mw) of the fluororesin is preferably 100,0000 to 5,000,000, more preferably 200,000 to 3,000,000, in order to maintain a good balance between resistance and adhesion and resin viscosity.
- Mw weight average molecular weight
- 500,000 to 1,500,000 is more preferable.
- the glass transition point of the fluororesin is preferably 20° C. or lower, more preferably 10° C. or lower, and even more preferably 0° C. or lower, from the viewpoint of the film-forming properties of the electrode film.
- Examples of commercial products of polyvinylidene fluoride and modified products thereof include KF polymer series "W#7300, W#7200, W#1700, W#1300, W#1100, W#9700, W#” manufactured by Kureha Co., Ltd. 9300, W # 9100, L # 7305, L # 7208, L # 1710, L # 1320, L # 1120", Solvay's solef series "6008, 6010, 6012, 1015, 6020, 5130, 9007, 460, 41308 , 11010, 21510, 31508, 60512" (all are trade names).
- the resin composition may contain a binder resin other than the fluororesin and the resin-type dispersant.
- binder resins are not particularly limited as long as they are usually used as binder resins for paints, and can be appropriately selected according to the purpose.
- the binder resin used in the resin composition is preferably a resin capable of bonding substances such as active materials and CNTs.
- the binder resin used in the resin composition is, for example, a polymer or copolymer containing ethylene, propylene, vinyl chloride, vinyl acetate, maleic acid, acrylic acid, acrylic acid ester, methacrylic acid, methacrylic acid ester, styrene, etc. as structural units.
- Coalescence Polyurethane resin, polyester resin, phenol resin, epoxy resin, phenoxy resin, urea resin, melamine resin, alkyd resin, acrylic resin, formaldehyde resin, silicone resin; styrene-butadiene rubber, elastomer such as fluororubber; polyaniline, polyacetylene and conductive resins such as Modified products, mixtures, and copolymers of these resins may also be used, and may be used singly or in combination of two or more.
- the resin composition contains carbon nanotubes, a dispersant, a fluororesin, and a dispersion medium.
- the resin composition may optionally contain other additives such as wetting agents, surfactants, pH adjusters, wetting and penetrating agents, and leveling agents, other conductive materials, and resin components such as other binder resins. Ingredients may be included as appropriate to the extent that the objects of the present invention are not impaired.
- the optional component can be added at any timing such as before preparation of the resin composition, during mixing, after mixing, or a combination thereof.
- the resin composition for a secondary battery electrode is in a state before the active material is added. In this respect, the resin composition for a secondary battery electrode is distinguished from a mixture slurry containing an active material.
- the resin composition for secondary battery electrodes does not substantially contain an active material.
- This is a concept excluding the state in which the active material is intentionally added to the resin composition for secondary battery electrodes, and the active material is 1% by mass or less with respect to the total mass of the resin composition for secondary battery electrodes, and 0 0.5% by mass or less, or 0.1% by mass or less, or 0% by mass.
- the active material is as described later.
- the dispersibility of CNTs in a resin composition can be evaluated by the complex elastic modulus and phase angle obtained by dynamic viscoelasticity measurement.
- the complex elastic modulus and phase angle of the resin composition are measured values at 25° C. and a frequency of 1 Hz. Specifically, it can be measured by the method described in Examples.
- the complex elastic modulus of the resin composition indicates the hardness of the resin composition, and tends to decrease as the dispersibility of CNTs improves and as the viscosity of the resin composition decreases.
- the complex elastic modulus may be high due to the structural viscosity of the CNT itself.
- the entanglement of CNTs, dispersant, fluororesin, and other resin components, or the influence of intermolecular forces among these also changes.
- the phase angle may be a low numerical value.
- the complex elastic modulus also changes depending on the entanglement of CNTs, dispersant, fluororesin, and other resin components, or the influence of intermolecular forces among these, in the same manner as the complex elastic modulus.
- the product (X ⁇ Y) of the complex elastic modulus X (Pa) and the phase angle Y (°) is 30 or more and 5,000 or less, so that the resin composition has a high concentration and high fluidity.
- an electrode film having very good conductivity can be obtained.
- the product (X ⁇ Y) of the complex elastic modulus X (Pa) and the phase angle Y (°) is preferably 30 or more, more preferably 50 or more, even more preferably 100 or more, and 500 It is more preferable that it is above. Also, it is preferably 5,000 or less, more preferably 3,000 or less, still more preferably 1,500 or less, and even more preferably 1,000 or less.
- the median diameter ( ⁇ m) of the resin composition is preferably 40 ⁇ m or less, more preferably 35 ⁇ m or less. Furthermore, the median diameter ( ⁇ m) of the resin composition is preferably 0.4 ⁇ m or more, preferably 5.0 ⁇ m or less, and more preferably 2.0 ⁇ m or less.
- a resin composition in an appropriate dispersed state can be obtained by setting the amount within the above range. If the temperature is below the above range, aggregated CNTs will be present, and if the above range is exceeded, a large number of finely cut CNTs will be generated, making it difficult to form an efficient conductive network.
- CNT dispersion efficiency it is preferable to mix and disperse CNTs, a dispersant, and a dispersion medium to prepare a CNT dispersion, and then mix the CNT dispersion with the fluororesin.
- the method of adding the fluororesin to the CNT dispersion is not particularly limited, but for example, powdery fluororesin may be added to the CNT dispersion and mixed.
- a varnish obtained by dissolving a fluororesin in a non-aqueous solvent may be added to and mixed with the CNT dispersion.
- the non-aqueous solvent for the varnish is not particularly limited, and any one that can be used for the resin composition may be used.
- Dispersing devices include kneaders, two-roll mills, three-roll mills, planetary mixers, ball mills, horizontal sand mills, vertical sand mills, annular bead mills, attritors, high shear mixers, high pressure homogenizers, and ultrasonic homogenizers. .
- a high-shear mixer in the initial stage of dispersion from the viewpoint of promoting wetting of the CNTs and dissolving coarse particles, and then using a high-pressure homogenizer from the viewpoint of dispersing the CNTs while maintaining the aspect ratio.
- the dispersibility of CNTs can be further enhanced by using a high-pressure homogenizer to disperse the CNTs in multiple stages. Further, by dispersing with a bead mill after dispersing with a high-pressure homogenizer, it is possible to homogenize the dispersed state while maintaining the fiber length.
- the pressure when using a high-pressure homogenizer is preferably 60-150 MPa, more preferably 60-120 MPa.
- Dispersion methods using a dispersing device include batch-type dispersion, pass-type dispersion, circulation dispersion, etc. Any method may be used, and two or more methods may be combined.
- Batch-type dispersion is a method in which dispersion is carried out only by the main body of a dispersion device without using pipes or the like. Since it is easy to handle, it is preferable when manufacturing small quantities.
- Pass-type dispersion is a dispersing method in which a dispersing apparatus main body is provided with a tank for supplying a liquid to be dispersed and a tank for receiving the liquid to be dispersed through a pipe, and the dispersing apparatus main body is passed through.
- the dispersion treatment of the CNT dispersion is preferably carried out until the viscosity of the CNT dispersion is sufficiently lowered.
- the CNT dispersion after dispersion preferably has a viscosity of 10 mPa s or more and less than 10,000 mPa s when measured at 60 rpm at 25° C. using a Brookfield viscometer, and preferably 10 mPa s or more and less than 5,000 mPa s. more preferably 10 mPa ⁇ s or more and less than 2000 mPa ⁇ s, and even more preferably 10 mPa ⁇ s or more and less than 1000 mPa ⁇ s.
- the active material may be a positive electrode active material or a negative electrode active material.
- the positive electrode active material and the negative electrode active material may be simply referred to as "active material”.
- An active material is a material that serves as a base for battery reactions. Active materials are classified into positive electrode active materials and negative electrode active materials according to the electromotive force.
- the mixture slurry is preferably in slurry form in order to improve uniformity and workability.
- Oxide powder (eg Li x FePO 4 , Li x Fe 1-y Mny PO 4 , Li x CoPO 4 etc.), manganese oxide, iron oxide, copper oxide, nickel oxide, vanadium oxide (eg V 2 O 5 , V 6 O 13 ), transition metal oxide powders such as titanium oxide, transition metal sulfide powders such as iron sulfate (Fe 2 (SO 4 ) 3 ), TiS 2 and FeS.
- x, y, and z are numbers, 0 ⁇ x ⁇ 1, 0 ⁇ y ⁇ 1, 0 ⁇ z ⁇ 1, 0 ⁇ y+z ⁇ 1.
- These positive electrode active materials can also be used singly or in combination.
- active materials containing Ni and/or Mn are Elution tends to increase basicity, and this effect tends to cause gelation of the binder resin and deterioration of the dispersed state. Therefore, in the case of batteries containing active materials containing Ni and / or Mn, this Morphology is particularly effective.
- the electrode film is formed by forming a mixture slurry into a film, and contains CNTs, a dispersant, a fluororesin, and an active material.
- the electrode film may further contain optional components.
- the electrode film can be obtained by adding an active material to the resin composition described above to prepare a mixed material slurry, and coating the mixed material slurry.
- the electrode film can be formed by coating a mixture slurry on a current collector and removing volatile matter.
- the secondary battery preferably contains a separator.
- the separator include, but are not limited to, polyethylene nonwoven fabric, polypropylene nonwoven fabric, polyamide nonwoven fabric, and nonwoven fabric obtained by subjecting these to hydrophilic treatment.
- H-NBR1 had a Mooney viscosity (ML 1+4 , 100° C.) of 44 (measured according to Japanese Industrial Standard JIS K6300-1 at a temperature of 100° C. using an L-shaped rotor). Further, the hydrogenation rate (calculated from infrared spectroscopic analysis by total reflection measurement) was 0.7%. The structural unit derived from acrylonitrile determined from the 1 H-NMR quantitative spectrum was 32%.
- Batch-type dispersion was carried out with a grind gauge having a depth of 300 ⁇ m until the dispersed particle size became 250 ⁇ m or less. At this time, the dispersed particle size confirmed with a grind gauge was 180 ⁇ m. Subsequently, the liquid to be dispersed was supplied from the stainless container to a high-pressure homogenizer (Starburst Lab HJP-17007, manufactured by Sugino Machine Co., Ltd.) through a pipe, and circulating dispersion treatment was performed. The dispersion treatment was performed using a single nozzle chamber with a nozzle diameter of 0.25 mm and a pressure of 100 MPa.
- a high-pressure homogenizer Starburst Lab HJP-17007, manufactured by Sugino Machine Co., Ltd.
- Example 1-2-7 A carbon nanotube dispersion was prepared in the same manner as in Example 1-18, except that no binder was added. After that, after putting 100 parts of the carbon nanotube dispersion in a stainless steel container, 80 parts of the single-walled CNT resin composition (TUBALL-F) prepared in Production Example 4 was added to 100 parts of the carbon nanotube dispersion, The resin composition 27 was obtained by stirring with a disper until uniform.
- TABALL-F single-walled CNT resin composition
- Example 1-28 According to the materials and compositions shown in Table 1, resin compositions were prepared as follows. NMP was placed in a stainless container and heated to 50°C. After the dispersant and additive were added while stirring with a disper, the mixture was stirred for 1 hour to dissolve the dispersant. After tumbling the CNTs and binder in a powder state, they are added to the dispersant solution while stirring with a disper, and a high shear mixer (L5M-A, manufactured by SILVERSON) equipped with a square hole high shear screen is rotated at 8,000 rpm. Batch-type dispersion was carried out until the entire dispersion became uniform at a speed of . Then, in the same manner as in the carbon nanotube dispersion preparation process of Example 1-1, a pass-type dispersion treatment was performed using a high-pressure homogenizer to obtain a resin composition 28.
- a high shear mixer L5M-A, manufactured by SILVERSON
- resin compositions were prepared as follows. NMP was placed in a stainless container and heated to 50°C. After adding the dispersant, additive and binder while stirring with a disper, they were dissolved by stirring for 1 hour. Add CNT to the dispersant solution while stirring with a disper, attach a high shear mixer (L5M-A, manufactured by SILVERSON) with a square hole high shear screen, and make the whole uniform at a speed of 8,000 rpm, and the groove Batch-type dispersion was performed with a grind gauge having a maximum depth of 300 ⁇ m until the dispersed particle size became 250 ⁇ m or less. Then, in the same manner as in the carbon nanotube dispersion preparation process of Example 1-1, a pass-type dispersion treatment was performed using a high-pressure homogenizer to obtain a resin composition 32.
- a high shear mixer L5M-A, manufactured by SILVERSON
- Comparative Example 1-2 Comparative resin composition 2 was obtained in the same manner as in Examples 1-13 according to the materials and compositions shown in Table 1, except that the number of passes of the high-pressure homogenizer was changed to 15 times.
- the TI value was obtained by dividing the viscosity (mPa ⁇ s) at 60 rpm by the viscosity (mPa ⁇ s) at 6 rpm.
- Initial viscosity Criteria ⁇ : less than 1,000 mPa s ⁇ : 1,000 mPa s or more and less than 2,000 mPa s ⁇ : 2,000 mPa s or more and less than 10,000 mPa s ⁇ : 10,000 mPa s or more
- sedimentation Or separation TI value Judgment criteria ⁇ : less than 3.0 ⁇ : 3.0 or more and less than 5.0 ⁇ : 5.0 or more and less than 10.0 ⁇ : 10.0 or more, sedimentation or separation
- the median diameter was measured using a particle size distribution analyzer (Partical LA-960V2, manufactured by HORIBA).
- the operating conditions for circulation/ultrasound were as follows: circulation speed: 3; ultrasonic intensity: 7; ultrasonic duration: 1 minute; stirring speed: 1; stirring mode: continuous. Further, during air venting, ultrasonic operation was performed with an ultrasonic intensity of 7 and an ultrasonic duration of 5 seconds.
- the NMP has a refractive index of 1.470, and the carbon material has a refractive index of 1.92.
- the measurement was performed after diluting the measurement sample so that the transmittance of the red laser diode was 60 to 80%, and the volume was used as the particle size standard.
- ⁇ Evaluation of positive electrode> (Method for evaluating conductivity of positive electrode)
- the surface resistivity ( ⁇ / ⁇ ) of the mixture layer of the obtained positive electrode was measured using Loresta GP, MCP-T610 manufactured by Mitsubishi Chemical Analytic Tech. After the measurement, the thickness of the mixture layer was multiplied to obtain the volume resistivity ( ⁇ cm) of the positive electrode.
- the thickness of the composite layer is obtained by subtracting the thickness of the aluminum foil from the average value obtained by measuring three points in the electrode using a film thickness gauge (DIGIMICRO MH-15M manufactured by NIKON), and obtaining the volume resistivity of the positive electrode ( ⁇ cm).
- an electrolytic solution ethylene carbonate, dimethyl carbonate, and diethyl carbonate were mixed at a volume ratio of 1:1:1 to prepare a mixed solvent, and as an additive, vinylene carbonate After adding 1 part by mass with respect to 100 parts by mass of LiPF 6 , 2 mL of a non-aqueous electrolyte in which LiPF 6 was dissolved at a concentration of 1 M) was injected, and then the aluminum laminate was sealed to prepare a secondary battery.
- an electrolytic solution ethylene carbonate, dimethyl carbonate, and diethyl carbonate were mixed at a volume ratio of 1:1:1 to prepare a mixed solvent, and as an additive, vinylene carbonate After adding 1 part by mass with respect to 100 parts by mass of LiPF 6 , 2 mL of a non-aqueous electrolyte in which LiPF 6 was dissolved at a concentration of 1 M) was injected, and then the aluminum laminate was sealed to prepare a secondary battery.
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Abstract
Description
<1>カーボンナノチューブと、分散剤と、フッ素樹脂と、分散媒とを含み、活物質を含まず、動的粘弾性測定による25℃及び1Hzでの複素弾性率X(Pa)と位相角Y(°)の積(X×Y)が30以上5,000以下である、二次電池電極用樹脂組成物。
<2>動的粘弾性測定による25℃及び1Hzでの複素弾性率が0.1Pa以上300Pa以下である、<1>記載の二次電池電極用樹脂組成物。
<3>動的粘弾性測定による25℃及び1Hzでの位相角が3°以上90°以下である、<1>または<2>記載の二次電池電極用樹脂組成物。
<5>前記カーボンナノチューブに対する前記分散剤の質量比が0.01以上2以下である、<1>から<4>のいずれかに記載の二次電池電極用樹脂組成物。
<6>前記カーボンナノチューブに対する前記フッ素樹脂の質量比が0.1以上10以下である、<1>から<5>のいずれかに記載の二次電池電極用樹脂組成物。
<7>前記カーボンナノチューブは、単層カーボンナノチューブと多層カーボンナノチューブとを含む、<1>から<6>のいずれかに記載の二次電池電極用樹脂組成物。
<9><1>から<8>のいずれかに記載の二次電池電極用樹脂組成物に、活物質を添加することを含む、二次電池電極用合材スラリーの製造方法。
<10>前記二次電池電極用樹脂組成物へ活物質を添加する前、後、同時、又はこれらの組み合わせにおいてカーボンブラックをさらに添加することを含む、<9>に記載の二次電池電極用合材スラリーの製造方法。
<12>正極、負極、及び電解質を含む二次電池の製造方法であって、<1>から<8>のいずれかに記載の二次電池電極用樹脂組成物に、活物質を添加し合材スラリーを作製すること、及び前記正極及び前記負極のうち少なくとも一方を、前記合材スラリーを集電体に塗工し電極膜を形成して作製することを含む、二次電池の製造方法。
二次電池電極用樹脂組成物は、カーボンナノチューブと、分散剤と、フッ素樹脂と、分散媒とを含み、さらに任意成分が含まれてもよい。カーボンナノチューブ(CNT)は、導電材として機能する。樹脂組成物には、カーボンナノチューブ以外の導電材が含まれてもよい。その他の導電材としては、例えば、カーボンブラック、フラーレン、グラフェン、多層グラフェン、グラファイト等の炭素材料等が挙げられる。CNT以外の導電材を用いる場合、分散剤の吸着性能の観点から、カーボンブラックが好ましく、例えばアセチレンブラック、ファーネスブラック、中空カーボンブラック、ケッチェンブラック等のカーボンブラックが挙げられる。これらのカーボンブラックは、中性、酸性、塩基性のいずれでもよく、酸化処理されたカーボンブラックや、黒鉛化処理されたカーボンブラックを使用してもよい。その他の導電材は、1種または2種以上併用して用いてもよい。
樹脂組成物は分散剤を含む。分散剤は、樹脂組成物中でCNTを分散安定化できるものが好ましい。分散剤は、樹脂型分散剤及び界面活性剤のいずれも使用することができるが、CNTへの吸着力が強く良好な分散安定性が得られることから、樹脂型分散剤が好ましい。カーボンナノチューブの分散に要求される特性に応じて適宜好適な種類の分散剤を、好適な配合量で使用することができる。
(2a)の方法では、重合体の調製に用いる分子量調整剤の使用量を増やすことでムーニー粘度を低下させる。
(2b)の方法では、塩基を添加して重合体のニトリル基含有構造単位に含まれるニトリル基を加水分解する等により変性させることで重合体のムーニー粘度を低下させる。
(2c)の方法では、重合体に、機械的なせん断力を負荷することでムーニー粘度を低下させる。
樹脂組成物は分散媒を含む。分散媒は、特に限定されないが、高誘電率溶媒であることが好ましく、高誘電率溶媒のいずれか1種からなる溶媒、または2種以上からなる混合溶媒を含むことが好ましい。また、高誘電率溶媒に、その他の溶媒を1種または2種以上混合して用いてもよい。
樹脂組成物はフッ素樹脂を含む。フッ素樹脂はフッ素を含む樹脂であり、耐熱性、耐薬品性、及び粘着性に優れ、バインダー樹脂として機能する。フッ素樹脂は、ポリエチレンの水素がフッ素またはトリフルオロメチルで置換された構造を備えるとよい。フッ素樹脂は、例えば、ポリテトラフルオロエチレン(PTFE)、ポリフッ化ビニル(PVF)、ポリフッ化ビニリデン(PVdF)、ポリクロロトリフルオロエチレン(PCTFE)等のホモポリマー;パーフルオロアルコキシアルカン(PFA)、パーフルオロエチレンプロペンコポリマー(FEP)、エチレン-テトラフルオロエチレンコポリマー(ETFE)、エチレン-クロロトリフルオロエチレンコポリマー(ECTFE)、テトラフルオロエチレン-パーフルオロジオキシソールコポリマー(TPE/PDD)等のコポリマー等が挙げられる。これらは1種単独で、または2種以上を組み合わせて用いてもよい。フッ素樹脂の中でも耐性面からポリテトラフルオロエチレン(PTFE)、ポリフッ化ビニル(PVF)、ポリフッ化ビニリデン(PVdF)、これらの構造単位を有する樹脂、これらの変性体、またはこれらの組み合わせが好ましい。なかでも、ポリフッ化ビニリデン系樹脂が好ましく、例えば、ポリフッ化ビニリデンのホモポリマー;フッ化ビニリデンとヘキサフルオロプロピレン、テトラフルオロエチレン等とのコポリマー等が挙げられる。ポリフッ化ビニリデン系樹脂は変性されていてもよく、例えばカルボキシ基等の酸性基が導入されていてもよい。フッ素樹脂は1種単独で、または2種以上を組み合わせて用いてもよい。
樹脂組成物は、カーボンナノチューブと、分散剤と、フッ素樹脂と、分散媒とを含む。樹脂組成物は、必要に応じて、湿潤剤、界面活性剤、pH調整剤、濡れ浸透剤、レベリング剤等のその他の添加剤、その他の導電材、その他のバインダー樹脂等の樹脂成分等の任意成分を、本発明の目的を阻害しない範囲で適宜含んでもよい。任意成分は、樹脂組成物作製前、混合時、混合後、又はこれらの組み合わせ等、任意のタイミングで添加することができる。二次電池電極用樹脂組成物は、活物質が添加される前の状態のものを意味する。この点において、二次電池電極用樹脂組成物は、活物質を含む合材スラリーと区別される。すなわち、二次電池電極用樹脂組成物は活物質を実質的に含まないものである。これは、二次電池電極用樹脂組成物に活物質が意図的に添加された状態を除く概念であり、二次電池電極用樹脂組成物の全質量に対し活物質は1質量%以下、0.5質量%以下、又は0.1質量%以下であればよく、あるいは0質量%であってよい。活物質については後述する通りである。
分散装置は、例えば、ニーダー、2本ロールミル、3本ロールミル、プラネタリーミキサー、ボールミル、横型サンドミル、縦型サンドミル、アニュラー型ビーズミル、アトライター、ハイシアミキサー、高圧ホモジナイザー、超音波ホモジナイザー等が挙げられる。なかでも、CNT分散液又は樹脂組成物中にCNTを微細に分散させ、好適な分散性を得るために、ハイシアミキサー、高圧ホモジナイザー、超音波ホモジナイザー、又はこれらを組み合わせて用いることが好ましい。特に、CNTの濡れを促進し、粗い粒子を解す観点から、分散の初期工程ではハイシアミキサーを用い、続いて、CNTのアスペクト比を保ったまま分散させる観点から、高圧ホモジナイザーを用いることが好ましい。高圧ホモジナイザーは循環分散によって多段階に行うことでCNTの分散性をより高めることができる。また、高圧ホモジナイザーで分散させたあと、さらにビーズミルにて分散させることで、繊維長を保ちつつ、分散状態を均一化させることができる。高圧ホモジナイザーを使用する際の圧力は60~150MPaが好ましく、60~120MPaであることがより好ましい。
以下、樹脂組成物を製造する際に用意されるカーボンナノチューブ分散液の一例について説明する。なお、上記した成分及び物性を備える樹脂組成物は、下記のCNT分散液を用いて製造されるものに限定されない。カーボンナノチューブ分散液は、カーボンナノチューブと、分散剤と、分散媒とを含み、任意成分を本発明の目的を阻害しない範囲で適宜含んでもよい。任意成分は、分散液作製前、分散時、分散後、又はこれらの組み合わせ等、任意のタイミングで添加することができる。任意成分としては、上記樹脂組成物で説明したものを用いることができる。
二次電池電極用合材スラリーは、上記した樹脂組成物に、活物質を添加することで得ることができる。合材スラリーは、必要に応じて、その他の任意成分を本発明の目的を阻害しない範囲で適宜含んでもよい。任意成分は、合材スラリー作製前、混合時、混合後、又はこれらの組み合わせ等、任意のタイミングで添加することができる。任意成分は、上記樹脂組成物で説明したものであってよい。
正極活物質は、特に限定されないが、例えば、二次電池用途は、リチウムイオンを可逆的にドーピングまたはインターカレーション可能な金属酸化物および金属硫化物等の金属化合物を使用することができる。例えば、リチウムマンガン複合酸化物(例えばLixMn2O4またはLixMnO2)、リチウムニッケル複合酸化物(例えばLixNiO2)、リチウムコバルト複合酸化物(LixCoO2)、リチウムニッケルコバルト複合酸化物(例えばLixNi1-yCoyO2)、リチウムマンガンコバルト複合酸化物(例えばLixMnyCo1-yO2)、リチウムニッケルマンガンコバルト複合酸化物(例えばLixNiyCozMn1-y-zO2)、スピネル型リチウムマンガンニッケル複合酸化物(例えばLixMn2-yNiyO4)等のリチウムと遷移金属との複合酸化物粉末、オリビン構造を有するリチウムリン酸化物粉末(例えばLixFePO4、LixFe1-yMnyPO4、LixCoPO4など)、酸化マンガン、酸化鉄、酸化銅、酸化ニッケル、バナジウム酸化物(例えばV2O5、V6O13)、酸化チタン等の遷移金属酸化物粉末、硫酸鉄(Fe2(SO4)3)、TiS2、およびFeS等の遷移金属硫化物粉末等が挙げられる。ただし、x、y、zは、数であり、0<x<1、0<y<1、0<z<1、0<y+z<1である。これら正極活物質は、1種または複数を組み合わせて使用することもできる。これらの活物質の中でも、特に、Niおよび/またはMnを含有する活物質は(遷移金属中のNiおよび/またはMnの合計量が50mol%以上の場合は殊更)、原料由来成分または金属イオンの溶出によって、塩基性が高くなる傾向があり、その影響によってバインダー樹脂のゲル化や分散状態の悪化が起こりやすいことから、Niおよび/またはMnを含有する活物質を含有する電池の場合、本実施形態が特に有効である。
負極活物質は、特に限定されないが、例えば、リチウムイオンを可逆的にドーピングまたはインターカレーション可能な金属Li、またはその合金、スズ合金、シリコン合金負極、LiXTiO2、LiXFe2O3、LiXFe3O4、LiXWO2等の金属酸化物系、ポリアセチレン、ポリ-p-フェニレン等の導電性高分子、高黒鉛化炭素材料等の人造黒鉛、あるいは天然黒鉛等の炭素質粉末、樹脂焼成炭素材料を用いることができる。ただし、xは数であり、0<x<1である。これら負極活物質は、1種または複数を組み合わせて使用することもできる。特にシリコン合金負極を用いる場合、理論容量が大きい反面、体積膨張が極めて大きいため、高黒鉛化炭素材料等の人造黒鉛、あるいは天然黒鉛等の炭素質粉末、樹脂焼成炭素材料等と組み合わせて用いるのが好ましい。
電極膜は、合材スラリーを膜状に形成してなるものであり、CNT、分散剤、フッ素樹脂、及び活物質を含む。電極膜には、任意成分がさらに含まれてもよい。電極膜は、上記した樹脂組成物に活物質を添加し合材スラリーを作製し、合材スラリーを塗工することで得ることができる。例えば、電極膜は、合材スラリーを集電体上に塗工し揮発分を除去することで形成することができる。
二次電池は、正極と、負極と、電解質とを含み、正極及び負極からなる群から選択される少なくとも1つが上記した電極膜を含む。二次電池の製造方法では、例えば、正極及び負極のうち少なくとも一方は、合材スラリーを集電体に塗工し電極膜を形成して作製され、合材スラリーは、上記した二次電池電極用樹脂組成物に活物質を添加して作製される。
(製造例1 H-NBR1の製造)
ステンレス製重合反応器に、アクリロニトリル32部、1,3-ブタジエン68部、オレイン酸カリ石ケン3部、アゾビスイソブチロニトリル0.3部、t-ドデシルメルカプタン0.48部、及びイオン交換水200部を加えた。窒素雰囲気下において、撹拌しながら、45℃で20時間の重合を行い、転化率90%で重合を終了した。未反応のモノマーを減圧ストリッピングにより除き、固形分濃度約30%のアクリロニトリル-共役ジエン系ゴムラテックスを得た。続いて、ラテックスにイオン交換水を追加して全固形分濃度を12%に調整し、容積1Lの撹拌機付きオートクレーブに投入して、窒素ガスを10分間にわたり流して内容物中の溶存酸素を除去した。水素化触媒としての酢酸パラジウム75mgを、パラジウムに対して4倍モルの硝酸を添加したイオン交換水180mLに溶解して調製した触媒液を、オートクレーブに添加した。オートクレーブ内を水素ガスで2回置換した後、3MPaまで水素ガスで加圧した状態でオートクレーブの内容物を50℃に加温し、6時間の水素化反応を行った。その後、内容物を常温に戻し、オートクレーブ内を窒素雰囲気とした後、固形分を乾燥させて分散剤(H-NBR1)を得た。H-NBR1のムーニー粘度(ML1+4、100℃)(日本工業規格JIS K6300-1に準拠して温度100℃でL形ローターを使用して測定した)は、44であった。また、水素添加率(全反射測定法による赤外分光分析から算出)は0.7%であった。1H-NMR定量スペクトルから求めたアクリロニトリル由来の構造単位は32%であった。
特開2020-163362号公報の段落(0078)に記載の分散剤(A-6:アクリロニトリル/ヒドロキシエチルアクリレート=90/10、重量平均分子量15,000)を製造した。得られた分散剤は、以下、PANと表記する。
(製造例3 100T-Pの製造)
カーボンナノチューブ(K-Nanos 100T:Kumho Petrochemical製)1gに対して、水5gを加えた後、ヘンシェル型ミキサーで撹拌し、粒状のカーボンナノチューブ(粒径約7mm)を得た。粒状のカーボンナノチューブをバットに広げ、100℃の減圧熱風オーブンにて7時間乾燥させ圧縮CNTを得た。得られた圧縮CNTをセラミック製のるつぼに入れ、焼成炉内に配置した。炉内を1Torr以下となるまで真空廃棄してから1000℃まで昇温させた。炉内の圧力が90Torrとなるまで毎分0.3Lの四塩化炭素ガスを導入した後、炉内の温度を1600℃まで昇温して1時間保持した。続いて、ヒーターを停止してからゆっくり1Torrになるまで減圧し、室温になるまで放冷しした。炉内の減圧を解除して、るつぼから高純度化処理したカーボンナノチューブ(100T-P)を回収した。
(製造例4 TUBALL-Fの製造)
ステンレス容器にN-メチル-2-ピロリドン(NMP)97.6部を加えて、ディスパーで撹拌しながら、ポリフッ化ビニリデン樹脂(solef5130、solvay製)2.0部を加えて、ディスパーでポリフッ化ビニリデン樹脂が溶解するまで撹拌した。その後、単層カーボンナノチューブ(TUBALL:OCSiAl製、炭素純度93%)0.4部を計量し、ディスパーで撹拌しながら添加して、ハイシアミキサー(L5M-A、SILVERSON製)に角穴ハイシアスクリーンを装着し、8,600rpmの速度で全体が均一になるまでバッチ式分散を行った。続いて、ステンレス容器から、配管を介して高圧ホモジナイザー(スターバーストラボHJP-17007、スギノマシン製)に被分散液を供給し、パス式分散処理を5回行い、単層カーボンナノチューブ樹脂組成物(TUBALL-F)を得た。分散処理はシングルノズルチャンバーを使用し、ノズル径0.25mm、圧力60MPaにて行った。
・H-NBR2:Therban(R)3406(ARLANXEO製、水素化アクリロニトリル-ブタジエンゴム)
・H-NBR3:Therban(R)AT 3404(ARLANXEO製、水素化アクリロニトリル-ブタジエンゴム)
・H-NBR4:Zetpole2000L(日本ゼオン製、水素化アクリロニトリル-ブタジエンゴム)
・PVP:ポリビニルピロリドンK-15(ISP製)
・PVA:クラレポバール3-86SD(クラレ製、変性ポリビニルアルコール)
・100T:K-Nanos 100T(Kumho Petrochemical製、多層CNT、平均外径13nm、比表面積210m2/g)
・BT1001M:LUCAN BT1001M(LG chem Ltd製、多層CNT、平均外径13nm、比表面積250m2/g)
・10B:JENOTUBE10B(JEIO製、多層CNT、平均外径10nm、比表面積230m2/g)
・8B:JENOTUBE8B(JEIO製、多層CNT、平均外径8nm、比表面積300m2/g)
・6A:JENOTUBE6A(JEIO製、多層CNT、平均外径6nm、比表面積700m2/g)
・TUBALL:単層カーボンナノチューブ(OCSiAl製、平均外径1.6nm、炭素純度93%、比表面積975m2/g)
・Super-P(IMERYSGraphite&Carbon社製、導電性カーボンブラック、BET比表面積62m2/g)
・S-5130:solef5130(solvay製、ポリフッ化ビニリデン樹脂)
・W#7300:KFポリマーW#7300(クレハ製、ポリフッ化ビニリデン樹脂)
・W#7200:KFポリマーW#7200(クレハ製、ポリフッ化ビニリデン樹脂)
・W#1300:KFポリマーW#1300(クレハ製、ポリフッ化ビニリデン樹脂)
・W#9300:KFポリマーW#9300(クレハ製、ポリフッ化ビニリデン樹脂)
(実施例1-1)
表1に示す材料と組成に従い、バインダーを除く材料を順次添加し、以下の通りカーボンナノチューブ分散液を作製した。まず、ステンレス容器にNMPをとり、50℃に加温した。ディスパーで撹拌しながら分散剤、添加剤を添加した後、1時間撹拌して、分散剤を溶解させた。続いて、CNTをディスパーで撹拌しながら添加して、ハイシアミキサー(L5M-A、SILVERSON製)に角穴ハイシアスクリーンを装着し、8,000rpmの速度で全体が均一になり、溝の最大深さ300μmのグラインドゲージにて分散粒度が250μm以下になるまでバッチ式分散を行った。このとき、グラインドゲージにて確認した分散粒度は180μmであった。続いて、ステンレス容器から、配管を介して高圧ホモジナイザー(スターバーストラボHJP-17007、スギノマシン製)に被分散液を供給し、循環式分散処理を行った。分散処理はシングルノズルチャンバーを使用し、ノズル径0.25mm、圧力100MPaにて行った。被分散液のB型粘度計(TOKI SANGYO製、VISCOMETER、MODEL:BL)で測定した60rpmにおける粘度が3,000mPa・s以下となるまで分散した後、高圧ホモジナイザーにて表1に示すパス回数に従いパス式分散処理を行い、カーボンナノチューブ分散液を得た。続いて、50℃に加温し、ディスパーで撹拌しながらバインダーを少量ずつ全量添加した。2時間撹拌し、バインダーを全量溶解させ、樹脂組成物1を得た。
表1に示す材料、組成、およびパス回数に従い変更した以外は、実施例1-1と同様にして樹脂組成物2~25を得た。樹脂組成物24の作製では、CNTを添加する際、6A及びTUBALLを同時に添加した。樹脂組成物25の作製では、CNTを添加する際、6A及びTUBALLとともにその他導電材のSuper-Pを同時に添加した。
バインダーを予めNMPに溶解し、8%溶液として用いた以外は、実施例1-1と同様にして樹脂組成物26を得た。なお、カーボンナノチューブ分散液を調製する際には、バインダー溶解に用いたNMPを控えておき、仕上がりの組成を合わせた。
バインダーを添加しなかったこと以外は、実施例1-18と同様の方法にてカーボンナノチューブ分散液を作製した。その後、前記カーボンナノチューブ分散液100部をステンレス容器に入れた後、製造例4で作製した単層CNT樹脂組成物(TUBALL-F)を前記カーボンナノチューブ分散液100部に対して80部加えて、ディスパーで均一になるまで撹拌して、樹脂組成物27を得た。
表1に示す材料と組成に従い、以下の通り樹脂組成物を作製した。ステンレス容器にNMPをとり、50℃に加温した。ディスパーで撹拌しながら分散剤、添加剤を添加した後、1時間撹拌して、分散剤を溶解させた。CNTとバインダーを粉末状態でタンブリングしてから、ディスパーで撹拌しながら前記分散剤溶液に添加して、ハイシアミキサー(L5M-A、SILVERSON製)に角穴ハイシアスクリーンを装着し、8,000rpmの速度で全体が均一になり、溝の最大深さ300μmのグラインドゲージにて分散粒度が250μm以下になるまでバッチ式分散を行った。以下、実施例1-1のカーボンナノチューブ分散液の作製工程と同様にして、高圧ホモジナイザーにてパス式分散処理を行い、樹脂組成物28を得た。
表1に示す分散剤を用いた以外は、実施例1-28と同様にして、樹脂組成物29~31を得た。
表1に示す材料と組成に従い、以下の通り樹脂組成物を作製した。ステンレス容器にNMPをとり、50℃に加温した。ディスパーで撹拌しながら分散剤、添加剤およびバインダーを添加した後、1時間撹拌して溶解させた。CNTをディスパーで撹拌しながら前記分散剤溶液に添加して、ハイシアミキサー(L5M-A、SILVERSON製)に角穴ハイシアスクリーンを装着し、8,000rpmの速度で全体が均一になり、溝の最大深さ300μmのグラインドゲージにて分散粒度が250μm以下になるまでバッチ式分散を行った。以下、実施例1-1のカーボンナノチューブ分散液の作製工程と同様にして、高圧ホモジナイザーにてパス式分散処理を行い、樹脂組成物32を得た。
表1に示す材料と組成に従い、高圧ホモジナイザーのパス回数を10回に変更した以外は、実施例1-1と同様にして比較樹脂組成物1を得た。
表1に示す材料と組成に従い、高圧ホモジナイザーのパス回数を15回に変更した以外は、実施例1-13と同様にして比較樹脂組成物2得た。
実施例1-1で、高圧ホモジナイザーを用いて分散した代わりに、ビーズミル(アシザワ製、スターミルLMZ06、ビーズ直径1.0mm、ビーズ充填率80%)を用いて分散し、比較樹脂組成物3を得た。なお、パス回数は25回とした。
・NaOH:水酸化ナトリウム(東京化成工業製、純度>98.0%、顆粒状)
・アミノエタノール:2-アミノエタノール(東京化成工業製、純度>99.0%)
・t-BuONa:ナトリウム-t-ブトキシド(東京化成工業製、純度>98.0%)
(粒度の測定方法)
樹脂組成物の粗大粒子の有無、粒度は、溝の最大深さ100μmのグラインドゲージを用い、JIS K5600-2-5に準ずる判定方法により求めた。
粒度 判定基準
◎:20μm未満
〇:20μm以上50μm未満
△:50μm以上90μm未満
×:90μm以上
樹脂組成物の粘度は、B型粘度計(東機産業製「BL」)を用いて、温度25℃にて、ヘラで充分に撹拌した後、直ちにB型粘度計ローター回転速度6rpmにて測定し、引き続き60rpmにて測定した。60rpmにて測定した粘度を初期粘度とした。低粘度であるほど分散性が良好であり、高粘度であるほど分散性が不良である。得られた分散液が明らかに分離や沈降しているものは分散性不良とした。また、60rpmにおける粘度(mPa・s)を、6rpmにおける粘度(mPa・s)で除した値からTI値を求めた。
初期粘度 判定基準
◎:1,000mPa・s未満
○:1,000mPa・s以上2,000mPa・s未満
△:2,000mPa・s以上10,000mPa・s未満
×:10,000mPa・s以上、沈降または分離
TI値 判定基準
◎:3.0未満
○:3.0以上5.0未満
△:5.0以上10.0未満
×:10.0以上、沈降または分離
光沢測定用の試料は、樹脂組成物を平滑なガラス基板上に1mL滴下し、No.7のバーコーターにて2cm/秒で塗工した後、140℃の熱風オーブンで10分間焼き付け、放冷して得た。塗工面積は約10cm×10cmとした。光沢計(BYK Gardner製光沢計 micro-gross60°)を用い、端部を除く塗膜面内の3か所を無作為に選び、1回ずつ測定して平均値を60°における光沢とした。
光沢 判定基準
◎:30以上
○:20以上30未満
△:10以上20未満
×:10未満
メジアン径は粒度分布測定装置(Partical LA-960V2、HORIBA製)を用いて測定した。循環/超音波の動作条件は、循環速度:3、超音波強度:7、超音波時間:1分、撹拌速度:1、撹拌モード:連続とした。また、空気抜き中は超音波強度7、超音波時間5秒で超音波作動を行った。NMPの屈折率は1.470、カーボン材料の屈折率は1.92とした。測定は、測定試料を赤色レーザーダイオードの透過率が60~80%となるように希釈した後行い、粒子径基準は体積とした。
メジアン径 判定基準
○:0.4μm以上2.0μm未満
△:2.0μm以上5.0μm未満
×:0.4μm未満、または5.0μm以上
樹脂組成物の複素弾性率X及び位相角Yは、直径60mm、2°のコーンにてレオメーター(Thermo Fisher Scientific株式会社製RheoStress1回転式レオメーター)を用い、25℃、周波数1Hzにて、ひずみ率0.01%から5%の範囲で動的粘弾性測定を実施することで評価した。得られた複素弾性率が小さいほど分散性が良好であり、大きいほど分散性が不良である。また、得られた位相角が大きいほど分散性が良好であり、小さいほど分散性が不良である。さらに、得られた複素弾性率X(Pa)と位相角Y(°)の積(X×Y)を算出した。
ディスパーにて撹拌しながら樹脂組成物にNMPを少しずつ滴下し、50倍に希釈したものを、表面が平滑な基材に少量滴下し、乾燥させて観察用試料とした。得られた観察用試料を走査型電子顕微鏡にて観測するとともに撮像した。観測写真において、任意の300個のCNTを選び、それぞれの繊維長を計測して、平均値を算出し、平均繊維長とした。
貯蔵安定性の評価は、分散液を50℃にて7日間静置して保存した後の粘度を測定した。測定方法は初期粘度と同様の方法で測定した。
貯蔵安定性 判定基準
◎:初期同等
○:粘度がわずかに変化した
△:粘度が上昇したがゲル化はしていない
×:ゲル化している
(実施例2-1~2-37、比較例3-1~3-3)
表3に示す組み合わせと組成比に従い、以下のようにして正極合材スラリーおよび正極を作製した。容量150cm3のプラスチック容器に樹脂組成物と、正極活物質とを添加し、自転・公転ミキサー(シンキー製 あわとり練太郎、ARE-310)を用いて、2,000rpmで150秒間撹拌し、正極合材スラリーを得た。正極合材スラリーの不揮発分は68.17質量%とした。なお、実施例2-36では、表中に示す組成比にしたがって、容量150cm3のプラスチック容器に樹脂組成物と、正極活物質と、さらにバインダー(S-5130:solef5130(solvay製))とを添加した以外は、上記方法に従って正極36用の合材スラリーを作製した。また、実施例2-37では、表中に示す組成比にしたがって、容量150cm3のプラスチック容器に樹脂組成物と、正極活物質と、さらにその他導電材(Super-P(IMERYSGraphite&Carbon社製、導電性カーボンブラック))とを添加した以外は、上記方法に従って正極37用の合材スラリーを作製した。
・NMC1:セルシードNMC(LiNi0.6Co0.2Mn0.2O2、日本化学工業製)
・NMC2:S800(LiNi0.8Mn0.1Co0.1O2、金和製)
・NCA:NAT-7050(LiNi0.8Co0.15Al0.05O2、BASF戸田バッテリーマテリアルズ製)
・LFP:HED(商標)LFP-400(リン酸鉄リチウム、BASF製)
(正極の導電性評価方法)
得られた正極を、三菱化学アナリテック製:ロレスターGP、MCP-T610を用いて合材層の表面抵抗率(Ω/□)を測定した。測定後、合材層の厚みを乗算し、正極の体積抵抗率(Ω・cm)とした。合材層の厚みは、膜厚計(NIKON製、DIGIMICRO MH-15M)を用いて、電極中の3点を測定した平均値から、アルミ箔の膜厚を減算し、正極の体積抵抗率(Ω・cm)とした。
導電性 判定基準
◎:10Ω・cm未満
〇:10Ω・cm以上20Ω・cm未満
△:20Ω・cm以上30Ω・cm未満
×:30Ω・cm以上
得られた正極を、塗工方向を長軸として90mm×20mmの長方形に2本カットした。剥離強度の測定には卓上型引張試験機(東洋精機製作所製、ストログラフE3)を用い、180度剥離試験法により評価した。具体的には、100mm×30mmサイズの両面テープ(No.5000NS、ニトムズ製)をステンレス板上に貼り付け、作製した正極の合材層側を両面テープのもう一方の面に密着させ試験用試料とした。次いで、試験用試料を長方形の短辺が上下にくるように垂直に固定し、一定速度(50mm/分)でアルミ箔の末端を下方から上方に引っ張りながら剥離し、このときの応力の平均値を剥離強度とした。
密着性 判定基準
◎:0.8N/cm以上
○:0.5N/cm以上0.8N/cm未満
△:0.3N/cm以上0.5N/cm未満
×:0.3N/cm未満
(標準負極の作製)
容量150mlのプラスチック容器にアセチレンブラック(デンカブラック(登録商標)HS‐100、デンカ製)0.5部と、MAC500LC(カルボキシメチルセルロースナトリウム塩 サンローズ特殊タイプ MAC500L、日本製紙製、不揮発分100%)1部と、水98.4部とを加えた後、自転・公転ミキサー(シンキー製 あわとり練太郎、ARE-310)を用いて、2,000rpmで30秒間撹拌した。さらに活物質として人造黒鉛(CGB-20、日本黒鉛工業製)を97質量部添加し、自転・公転ミキサー(シンキー製 あわとり練太郎、ARE-310)を用いて、2,000rpmで150秒間撹拌した。続いてSBR(スチレンブタジエンゴム、TRD2001、不揮発分48%、JSR製)を3.1部加えて、自転・公転ミキサー(シンキー製 あわとり練太郎、ARE-310)を用いて、2,000rpmで30秒間撹拌し、標準負極合材スラリーを得た。標準負極合材スラリーの不揮発分は50質量%とした。
表4に記載した正極および標準負極を使用して、各々50mm×45mm、45mm×40mmに打ち抜き、打ち抜いた正極および標準負極と、その間に挿入されるセパレーター(多孔質ポリプロプレンフィルム)とをアルミ製ラミネート袋に挿入し、電気オーブン中、70℃で1時間乾燥した。その後、アルゴンガスで満たされたグローブボックス内で、電解液(エチレンカーボネートとジメチルカーボネートとジエチルカーボネートを体積比1:1:1の割合で混合した混合溶媒を作製し、さらに添加剤として、ビニレンカーボネートを100質量部に対して1質量部加えた後、LiPF6を1Mの濃度で溶解させた非水電解液)を2mL注入した後、アルミ製ラミネートを封口して二次電池をそれぞれ作製した。
得られた二次電池を25℃の恒温室内に設置し、充放電装置(北斗電工製、SM-8)を用いて充放電測定を行った。充電電流10mA(0.2C)にて充電終止電圧4.3Vで定電流定電圧充電(カットオフ電流1mA(0.02C))を行った後、放電電流10mA(0.2C)にて、放電終止電圧3Vで定電流放電を行った。この操作を3回繰り返した後、充電電流10mA(0.2C)にて充電終止電圧4.3Vで定電流定電圧充電(カットオフ電流(1mA0.02C))を行い、放電電流0.2Cおよび3Cで放電終止電圧3.0Vに達するまで定電流放電を行って、それぞれ放電容量を求めた。レート特性は0.2C放電容量と3C放電容量の比、以下の数式1で表すことができる。
(数式1) レート特性 = 3C放電容量/3回目の0.2C放電容量 ×100 (%)
レート特性 判定基準
◎:80%以上
○:60%以上80%未満
△:40%以上60%未満
×:40%未満
得られた二次電池を25℃の恒温室内に設置し、充放電装置(北斗電工製、SM-8)を用いて充放電測定を行った。充電電流25mA(0.5C)にて充電終止電圧4.3Vで定電流定電圧充電(カットオフ電流2.5mA(0.05C))を行った後、放電電流25mA(0.5C)にて、放電終止電圧3Vで定電流放電を行った。この操作を200回繰り返した。サイクル特性は25℃における3回目の0.5C放電容量と200回目の0.5C放電容量の比、以下の数式2で表すことができる。
(数式2)サイクル特性 = 3回目の0.5C放電容量/200回目の0.5C放電容量×100(%)
サイクル特性 判定基準
◎:85%以上
○:80%以上85%未満
△:50%以上80%未満
×:50%未満
Claims (12)
- カーボンナノチューブと、分散剤と、フッ素樹脂と、分散媒とを含み、活物質を含まず、動的粘弾性測定による25℃及び1Hzでの複素弾性率X(Pa)と位相角Y(°)の積(X×Y)が30以上5,000以下である、二次電池電極用樹脂組成物。
- 動的粘弾性測定による25℃及び1Hzでの複素弾性率が0.1Pa以上300Pa以下である、請求項1記載の二次電池電極用樹脂組成物。
- 動的粘弾性測定による25℃及び1Hzでの位相角が3°以上90°以下である、請求項1または2記載の二次電池電極用樹脂組成物。
- 前記カーボンナノチューブの含有量は、樹脂組成物の全量に対し、0.5質量%以上15質量%以下である、請求項1から3のいずれか1項に記載の二次電池電極用樹脂組成物。
- 前記カーボンナノチューブに対する前記分散剤の質量比が0.01以上2以下である、請求項1から4のいずれか1項に記載の二次電池電極用樹脂組成物。
- 前記カーボンナノチューブに対する前記フッ素樹脂の質量比が0.1以上10以下である、請求項1から5のいずれか1項に記載の二次電池電極用樹脂組成物。
- 前記カーボンナノチューブは、単層カーボンナノチューブと多層カーボンナノチューブとを含む、請求項1から6のいずれか1項に記載の二次電池電極用樹脂組成物。
- カーボンブラックをさらに含む、請求項1から7のいずれか1項に記載の二次電池電極用樹脂組成物。
- 請求項1から8のいずれか1項に記載の二次電池電極用樹脂組成物に、活物質を添加することを含む、二次電池電極用合材スラリーの製造方法。
- 前記二次電池電極用樹脂組成物へ活物質を添加する前、後、同時、又はこれらの組み合わせにおいてカーボンブラックをさらに添加することを含む、請求項9に記載の二次電池電極用合材スラリーの製造方法。
- 請求項1から8のいずれか1項に記載の二次電池電極用樹脂組成物に、活物質を添加し合材スラリーを作製すること、及び前記合材スラリーを塗工し電極膜を作製することを含む、電極膜の製造方法。
- 正極、負極、及び電解質を含む二次電池の製造方法であって、
請求項1から8のいずれか1項に記載の二次電池電極用樹脂組成物に、活物質を添加し合材スラリーを作製すること、及び
前記正極及び前記負極のうち少なくとも一方を、前記合材スラリーを集電体に塗工し電極膜を形成して作製することを含む、二次電池の製造方法。
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| JP2023534854A JP7687401B2 (ja) | 2021-07-14 | 2022-07-14 | 二次電池電極用樹脂組成物、二次電池電極用合材スラリーの製造方法、電極膜の製造方法、及び二次電池の製造方法 |
| KR1020237042082A KR20240005026A (ko) | 2021-07-14 | 2022-07-14 | 이차전지 전극용 수지 조성물, 이차전지 전극용 합재 슬러리의 제조방법, 전극막의 제조방법, 및 이차전지의 제조방법 |
| CA3221362A CA3221362A1 (en) | 2021-07-14 | 2022-07-14 | Resin composition for secondary battery electrodes, method for producing mixture slurry for secondary battery electrodes, method for producing electrode film, and method for producing secondary batter |
| US18/562,325 US20240243290A1 (en) | 2021-07-14 | 2022-07-14 | Resin composition for secondary battery electrodes, method for producing mixture slurry for secondary battery electrodes, method for producing electrode film, and method for producing secondary battery |
| EP22842175.6A EP4372839A1 (en) | 2021-07-14 | 2022-07-14 | Resin composition for secondary battery electrodes, method for producing mixture slurry for secondary battery electrodes, method for producing electrode film, and method for producing secondary battery |
| CN202280005162.7A CN116941061B (zh) | 2021-07-14 | 2022-07-14 | 二次电池电极用树脂组合物、二次电池电极用复合材浆料及电极膜及二次电池的制造方法 |
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| JP7414171B1 (ja) | 2023-03-10 | 2024-01-16 | 東洋インキScホールディングス株式会社 | カーボンナノチューブ分散組成物およびその利用 |
| WO2024204272A1 (ja) * | 2023-03-31 | 2024-10-03 | 日本ゼオン株式会社 | 複合材料および成形体 |
| JP7620126B1 (ja) | 2024-01-22 | 2025-01-22 | 大日精化工業株式会社 | カーボン材料分散液及びその使用 |
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| EP4372839A1 (en) | 2024-05-22 |
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