WO2018101134A1 - Binder composition for nonaqueous electrolyte battery electrode, hydrogel using binder composition as raw material, slurry composition for nonaqueous electrolyte battery electrode using same, nonaqueous electrolyte battery negative electrode, and nonaqueous electrolyte battery - Google Patents
Binder composition for nonaqueous electrolyte battery electrode, hydrogel using binder composition as raw material, slurry composition for nonaqueous electrolyte battery electrode using same, nonaqueous electrolyte battery negative electrode, and nonaqueous electrolyte battery Download PDFInfo
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- WO2018101134A1 WO2018101134A1 PCT/JP2017/041909 JP2017041909W WO2018101134A1 WO 2018101134 A1 WO2018101134 A1 WO 2018101134A1 JP 2017041909 W JP2017041909 W JP 2017041909W WO 2018101134 A1 WO2018101134 A1 WO 2018101134A1
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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
- H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
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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
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/052—Li-accumulators
- H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
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- 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 nonaqueous electrolyte battery electrode, a hydrogel using the same, a slurry composition for a nonaqueous electrolyte battery electrode using the same, a nonaqueous electrolyte battery negative electrode, and a nonaqueous electrolyte battery.
- Lithium ion secondary batteries are frequently used as secondary batteries used for the power sources of these portable terminals. Since portable terminals are required to have more comfortable portability, miniaturization, thinning, weight reduction, and high performance have rapidly progressed, and have come to be used in various places. This trend continues today, and batteries used in mobile terminals are further required to be smaller, thinner, lighter, and higher in performance.
- a non-aqueous electrolyte battery such as a lithium ion secondary battery has a positive electrode and a negative electrode installed via a separator, and LiPF 6 , LiBF 4 LiTFSI (lithium (bistrifluoromethylsulfonylimide)), LiFSI (lithium (bisfluorosulfonylimide). )) And a lithium salt dissolved in an organic liquid such as ethylene carbonate in a container.
- the negative electrode and the positive electrode are usually obtained by dissolving or dispersing a binder and a thickener in water and mixing an active material, a conductive aid (conductivity imparting agent) and the like with this, Hereinafter, it may be simply formed as a mixed layer by coating the current collector on the current collector and drying the water. More specifically, for example, for the negative electrode, a carbonaceous material capable of occluding and releasing lithium ions, which is an active material, and, if necessary, acetylene black, a conductive auxiliary agent, are secondary to a current collector such as copper. They are bound together by a binder for battery electrodes. On the other hand, for the positive electrode, LiCoO 2 that is an active material and, if necessary, a conductive aid similar to that of the negative electrode are bound to a current collector such as aluminum using a secondary battery electrode binder. Is.
- diene rubbers such as styrene-butadiene rubber and acrylics such as polyacrylic acid have been used as binders for aqueous media (for example, Patent Documents 1 and 2).
- the thickener include methylcellulose, ethylcellulose, hydroxyethylcellulose, hydroxypropoxycellulose, carboxymethylcellulose sodium salt (CMC-Na), sodium polyacrylate, etc.
- CMC-Na is often used.
- diene rubbers such as styrene-butadiene rubber have low adhesion to metal collectors such as copper, and there is a problem that the amount used cannot be reduced to increase the adhesion between the collector and the electrode material. .
- the capacity maintenance rate is low due to weakness against heat generated during charging and discharging.
- polyacrylic acid soda exhibits higher adhesion than styrene-butadiene rubber, but has a problem that the electrode is easily cracked because the electric resistance is high and the electrode becomes harder and less tough.
- demands for extending the usage time of mobile devices and shortening charging time have increased, and there is an urgent need to improve battery capacity (low resistance), life (cycle characteristics), and charging speed (rate characteristics). In particular, it is an obstacle. *
- the battery capacity is affected by the amount of active material, it is effective to suppress the amount of binder and thickener in order to increase the active material in a limited space of the battery.
- the rate characteristics are also affected by the ease of electron movement, it is effective to suppress the amount of binder and thickener that are non-conductive and prevent electron movement.
- the amount of the binder and the thickener is reduced, the binding property between the collector electrode and the electrode material and the active material in the electrode is lowered, and the durability (battery life) for long-term use is significantly reduced.
- the electrode becomes brittle. Thus, it has been difficult to improve battery characteristics such as battery capacity while maintaining the binding property between the collector electrode and the electrode material and maintaining the toughness as an electrode.
- the present invention has been made in view of the above-described problems, and an object thereof is to improve battery characteristics in a nonaqueous electrolyte battery without impairing the function as a binder, that is, the toughness as an electrode.
- Another object of the present invention is to improve battery characteristics in a non-aqueous electrolyte battery without impairing the binding property between the active materials and the collector electrode.
- the present inventors have found that the above object can be achieved by using a binder composition for a nonaqueous electrolyte battery electrode having the following constitution, and further investigation based on this finding Thus, the present invention was completed.
- the binder composition for a nonaqueous electrolyte battery electrode according to one aspect of the present invention (hereinafter also simply referred to as a binder composition) is an ⁇ -olefin-maleic acid copolymer obtained by copolymerizing an ⁇ -olefin and a maleic acid.
- a binder composition for a non-aqueous electrolyte battery electrode having a structure in which a neutralized salt of a coalescence is cross-linked with polyamines, and a viscosity of an aqueous solution containing 10% by weight of the binder composition at 25 ° C. and a shear rate of 40 s ⁇ 1 Is 1800 mPa ⁇ s to 15000 mPa ⁇ s.
- the binder composition for a nonaqueous electrolyte battery electrode according to this embodiment has a structure in which a neutralized salt of an ⁇ -olefin-maleic acid copolymer obtained by copolymerizing an ⁇ -olefin and a maleic acid is crosslinked with a polyamine.
- a binder composition for a non-aqueous electrolyte battery electrode, wherein an aqueous solution containing 10% by weight of the binder composition has a viscosity of 1800 mPa ⁇ s to 15000 mPa ⁇ s at 25 ° C. and a shear rate of 40 s ⁇ 1 . .
- a binder composition for a non-aqueous electrolyte battery electrode having binding properties and toughness can be obtained, and further, improvement of battery characteristics of the non-aqueous electrolyte battery can be realized using the binder composition. Can do.
- an ⁇ -olefin-maleic acid copolymer obtained by copolymerizing an ⁇ -olefin and a maleic acid is composed of a unit (A) based on the ⁇ -olefin and a unit (B) based on the maleic acid.
- the components (A) and (B) preferably satisfy (A) / (B) (molar ratio) of 1/1 to 1/3.
- a linear random copolymer having an average molecular weight of 10,000 to 500,000 is preferable.
- the unit (A) based on ⁇ -olefins is represented by the general formula —CH 2 CR 1 R 2 — (wherein R 1 and R 2 may be the same or different from each other, hydrogen Represents an alkyl or alkenyl group having 1 to 10 carbon atoms).
- the ⁇ -olefin used in this embodiment is a linear or branched olefin having a carbon-carbon unsaturated double bond at the ⁇ -position. In particular, olefins having 2 to 12 carbon atoms, particularly 2 to 8 carbon atoms are preferred.
- Representative examples that can be used include ethylene, propylene, n-butylene, isobutylene, n-pentene, isoprene, 2-methyl-1-butene, 3-methyl-1-butene, n-hexene, 2-methyl- 1-pentene, 3-methyl-1-pentene, 4-methyl-1-pentene, 2-ethyl-1-butene, 1,3-pentadiene, 1,3-hexadiene, 2,3-dimethylbutadiene, 2,5 -Pentadiene, 1,4-hexadiene, 2,2,4-trimethyl-1-pentene, styrene, ⁇ -methylstyrene, paramethylstyrene, methyl vinyl ether, ethyl vinyl ether and the like.
- isobutylene is particularly preferable from the viewpoints of availability, polysynthesis, and product stability.
- the isobutylene includes a mixture containing isobutylene as a main component, for example, a BB fraction (C4 fraction).
- BB fraction C4 fraction
- These olefins may be used alone or in combination of two or more.
- maleic anhydride maleic acid, maleic acid monoester (for example, methyl maleate, ethyl maleate, propyl maleate, phenyl maleate, etc.), maleic acid, as the unit (B) based on maleic acids
- Maleic anhydride derivatives such as diesters (eg dimethyl maleate, diethyl maleate, dipropyl maleate, diphenyl maleate etc.), maleic imides or N-substituted derivatives thereof (eg maleic imide, N-methylmaleimide, N N-substituted alkylmaleimides such as ethylmaleimide, N-propylmaleimide, Nn-butylmaleimide, Nt-butylmaleimide, N-cyclohexylmaleimide, N-phenylmaleimide, N-ethyl Phenyl male N-substituted alkylphenylmaleimide such as imide, or N-substi
- maleic anhydride is preferable from the viewpoint of availability, polymerization rate, and ease of molecular weight adjustment.
- These maleic acids may be used alone or in combination.
- Maleic acids are neutralized with alkali salts as described above, and the resulting carboxylic acid and carboxylic acid salt form a 1,2-dicarboxylic acid or salt form. This form has a function of capturing heavy metals eluted from the positive electrode.
- the content ratio of each structural unit in the copolymer of the present embodiment is preferably such that (A) / (B) is in the range of 1/1 to 1/3 in terms of molar ratio. This is because the advantages of hydrophilicity, water solubility, and affinity for metals and ions as a high molecular weight substance that dissolves in water can be obtained. Particularly, it is desirable that the molar ratio of (A) / (B) is 1/1 or a value close thereto, in which case the unit based on ⁇ -olefin, that is, —CH 2 CR 1 R 2 — A copolymer having a structure in which the units shown and units based on maleic acids are alternately repeated is obtained.
- the mixing ratio of ⁇ -olefins and maleic acids to obtain the copolymer of the present embodiment varies depending on the composition of the target copolymer, but ⁇ -olefin of 1 to 3 times the number of moles of maleic acids.
- Use of olefin is effective for increasing the reaction rate of maleic acids.
- the method for producing the copolymer of the present embodiment is not particularly limited, and for example, the copolymer can be obtained by radical polymerization.
- the polymerization catalyst used is an azo catalyst such as azobisisobutyronitrile, 1,1-azobiscyclohexane-1-carbonitrile, or an organic peroxide catalyst such as benzoyl peroxide or dicumyl peroxide. preferable.
- the amount of the polymerization catalyst used is required to be in the range of 0.1 to 5 mol%, preferably 0.5 to 3 mol% with respect to maleic acids.
- As a method for adding the polymerization catalyst and the monomer they may be added all at the beginning of the polymerization, but it is desirable to add them sequentially as the polymerization proceeds.
- the molecular weight can be appropriately adjusted mainly depending on the monomer concentration, the amount of catalyst used, and the polymerization temperature.
- the polymerization temperature is preferably 40 ° C.
- the polymerization time is usually preferably about 1 to 24 hours, more preferably 2 to 10 hours.
- the amount of the polymerization solvent used is preferably adjusted so that the concentration of the obtained copolymer is 5 to 40% by weight, more preferably 10 to 30% by weight.
- the copolymer of this embodiment usually has an average molecular weight of 10,000 to 500,000.
- a more preferred average molecular weight is 15,000 to 450,000.
- the average molecular weight of the copolymer of this embodiment is less than 10,000, the crystallinity is high and the adhesive strength between particles may be low.
- it exceeds 500,000 the solubility in water or a solvent becomes small, and it may precipitate easily.
- the average molecular weight of the copolymer of the present embodiment can be measured by, for example, a light scattering method or a viscosity method.
- the copolymer of this embodiment preferably has an intrinsic viscosity in the range of 0.05 to 1.5.
- the copolymer of this embodiment is usually obtained in the form of a powder having a grain size of about 16 to 60 mesh.
- the neutralized salt of a copolymer is a neutralized product in which active hydrogen of carbonyl acid generated from maleic acids reacts with a basic substance to form a salt.
- the basic substance may be any of a basic substance containing a monovalent metal and ammonia. It is preferred to use either or both.
- the neutralized salt of the ⁇ -olefin-maleic acid copolymer of the present embodiment is a neutralized salt with a basic substance containing a monovalent metal of ⁇ -olefin-maleic acid or ammonia of ⁇ -olefin-maleic acid. And a neutralized salt thereof or a mixture thereof.
- the degree of neutralization is not particularly limited, but when used as a binder, considering the reactivity with the electrolytic solution, it is usually 0.3 to 1 mol per carboxylic acid produced from maleic acids. It is preferably in the range of 1 mole, and more preferably neutralized in the range of 0.4 to 1 mole. With such a neutralization degree, it is possible to adjust the pH of the binder composition of the present embodiment to a predetermined range, and further, there is an advantage that the acidity is low and the electrolytic solution decomposition is suppressed.
- the degree of neutralization can be determined by a method such as titration with a base, an infrared spectrum, or an NMR spectrum.
- titration with a base can be performed.
- the specific titration method is not particularly limited, but it can be dissolved in water with little impurities such as ion-exchanged water, and a basic substance such as lithium hydroxide, sodium hydroxide, potassium hydroxide, It can be carried out by neutralization.
- the indicator for the neutralization point is not particularly limited, but an indicator such as phenolphthalein whose pH is indicated by a base can be used.
- the amount of the basic substance used is not particularly limited and is appropriately selected depending on the purpose of use and the like, but is usually 0.1 per mole of maleic acid units in the maleic acid copolymer.
- the amount is preferably ⁇ 2 mol. If it is such usage-amount, it will be possible to adjust pH of the binder composition of this embodiment to the predetermined range.
- the amount of the basic substance containing a monovalent metal is preferably 0.6 to 2.0 mol, more preferably 0.7 to 2. mol per mol of maleic acid unit in the maleic acid copolymer. When the amount is 0 mol, a water-soluble copolymer salt with little alkali residue can be obtained.
- the reaction between the ⁇ -olefin-maleic acid copolymer and the basic substance can be carried out according to a conventional method, but is carried out in the presence of water, and the neutralized product of the ⁇ -olefin-maleic acid copolymer is used as an aqueous solution.
- the method to obtain is simple and preferable.
- Examples of basic substances containing monovalent metals that can be used in the present embodiment include hydroxides of alkali metals such as sodium hydroxide, potassium hydroxide, and lithium hydroxide; alkali metals such as sodium carbonate and potassium carbonate. Carbonates of alkali metals such as sodium acetate and potassium acetate; phosphates of alkali metals such as trisodium phosphate, and the like.
- amines such as ammonia include primary amines such as ammonia, methylamine, ethylamine, butylamine and octylamine, secondary amines such as dimethylamine, diethylamine and dibutylamine, and tertiary amines such as trimethylamine, triethylamine and tributylamine. Is mentioned.
- ammonia, lithium hydroxide, sodium hydroxide, and potassium hydroxide are preferable as the basic substance.
- ammonia or lithium hydroxide as a binder for a lithium ion secondary battery.
- the basic substance containing monovalent metal and / or ammonia may be used alone or in combination of two or more.
- a neutralized product of an ⁇ -olefin-maleic acid copolymer using a basic substance containing an alkali metal hydroxide such as sodium hydroxide as long as the battery performance is not adversely affected. May be prepared.
- the non-aqueous electrolyte battery using the binder composition of the present embodiment is electrically Excellent properties.
- the binder composition of this embodiment further contains a crosslinking agent.
- a crosslinking agent By including a crosslinking agent, adhesiveness and toughness can be imparted to the binder composition.
- the binder composition of this embodiment contains polyamines as a crosslinking agent. That is, the binder composition of the present embodiment has a structure in which a neutralized salt of an ⁇ -olefin-maleic acid copolymer as described above is crosslinked with a polyamine.
- Any polyamine can be used as the cross-linking agent used in the present embodiment without limitation as long as it is electrochemically stable, and examples thereof include polyamines having a molecular weight of 500 or more. .
- high molecular weight polyamines include amino group-containing polymers, and preferred specific examples thereof include polyethyleneimine, polytetramethyleneimine, polyvinylamine, polyallylamine, polydiallylamine, polydimethylallylamine, dicyandiamide-formalin. Examples include condensates and dicyandiamide-alkylene (polyamine) condensates. These may be used alone or in combination. In view of availability and economy, it is preferable to use polyethyleneimine (PEI), polyallylamine, or polydiallylamine.
- PEI polyethyleneimine
- polyallylamine polydiallylamine
- the molecular weight of these polyamines is not particularly limited, and the average molecular weight is in the range of 500 to 50000, more preferably in the range of 1000 to 30000, and most preferably in the range of 1500 to 25000.
- the amount of polyamines to be added is not particularly limited, but is usually 0.05 to 30 parts by weight with respect to 100 parts by weight of ⁇ -olefin-maleic acid copolymer (solid content). Preferably, it is in the range of 0.3 to 10 parts by weight, most preferably in the range of 0.6 to 5 parts by weight. If the amount of polyamine added is in the range of 0.05 to 30 parts by weight, it is considered that the viscosity of the resulting binder composition can be easily adjusted to a desired range. Moreover, an excessively large addition amount is not preferable because the resistance component increases, and an excessively small addition amount is not preferable because adhesion and toughness cannot be imparted.
- the polyamines can be added simultaneously with the reaction of the ⁇ -olefin-maleic acid copolymer and a basic substance containing a monovalent metal, or the ⁇ -olefin-maleic acid copolymer and It can also be added after reacting a basic substance containing a monovalent metal.
- the ring-opening rate of the copolymer represents the hydrolysis rate of the site of maleic anhydride that is polymerized with ⁇ -olefins when maleic anhydride is used as the maleic acid.
- a preferable ring opening rate is 60 to 100%, more preferably 70% to 100%, and still more preferably 80 to 100%. If the ring-opening rate is too low, the structural freedom of the copolymer becomes small and the stretchability becomes poor, so that the force for adhering the electrode material particles to be bonded may be small, which is not preferable. Furthermore, there is a possibility that problems such as low affinity for water and poor solubility may occur.
- the ring-opening rate can be determined, for example, by measuring the hydrogen at the ⁇ -position of the maleic acid opened by 1H-NMR with reference to the hydrogen at the ⁇ -position of maleic anhydride.
- the ratio of the carbonyl group derived from the carbonyl group and the ring-opened maleic anhydride can also be determined by IR measurement.
- the neutralized salt of the copolymer means that the active hydrogen of the carbonyl acid generated by the ring opening of maleic anhydride is a basic substance as described above. It forms a salt by forming a salt.
- the degree of neutralization is not particularly limited. However, when used as a binder, considering the reactivity with the electrolytic solution, the degree of neutralization is 0. A range of 2 to 0.8 mol is preferable, and a neutralized range of 0.4 to 0.7 mol is more preferable. Such a neutralization degree has the advantage of low acidity and suppression of electrolyte decomposition.
- the degree of neutralization of the copolymer when maleic anhydride is used can be measured by the same method as described above.
- the aqueous solution of the binder composition containing 10% by weight of the neutralized salt has a viscosity at 25 ° C. and a shear rate of 40 s-1 as measured with a Brookfield viscometer. 1800 mPa ⁇ s to 15000 mPa ⁇ s. Further, the viscosity is more preferably in the range of 2000 mPa ⁇ s to 12000 mPa ⁇ s. By setting the viscosity in such a range, it is considered that the battery characteristics can be improved without impairing the binding property and toughness of the binder.
- the viscosity of the aqueous binder composition solution is adjusted, for example, by adjusting the molecular weight or neutralization degree of the copolymer, the addition amount or molecular weight of polyamines, or by adjusting the neutralization (pH) to be low.
- the amount can be adjusted to the above range by increasing the amount of carboxylic acid or by adding a thickener, but is not limited thereto.
- the viscosity in this embodiment can be measured by, for example, a rotational viscometer method.
- the binder composition of this embodiment is a hydrogel.
- water gels that are currently known to form hydrogels include water-soluble polymers such as starch, carrageenan, fiber derivatives, gelatin, casein, polyvinyl alcohol, polyvinyl pyrrolidone, polyacrylic acid, and polyoxyethylene oxide.
- Hydrogels using these water-soluble polymers are widely used in applications such as a fragrance material, a fireproof material, a heat insulation material, and a cold insulation material.
- hydrogels using these water-soluble polymers are generally complicated in their production methods. For example, a stepwise temperature adjustment is required (Japanese Patent Laid-Open No. 2013-234280, etc.), a gelation reaction under high temperature is required, or a stable hydrogel is formed unless the temperature is lower than 0 ° C.
- Production of hydrogel that can be easily gelled is a mainstream production method in which gelation reaction is not possible or it is necessary to promote gelation reaction by strictly adjusting pH of aqueous solution (JP 2009-536940 A, etc.)
- JP 2009-536940 A, etc. There are few ways.
- the gelation reaction is often slow, and the network structure cannot be sufficiently formed in a short time, and the desired performance may not be exhibited.
- a hydrogel obtained from the binder composition using the binder composition described above as a raw material is also included as a preferred embodiment. According to the present embodiment, it is possible to provide a hydrogel that is relatively simple in manufacturing method and can improve secondary battery characteristics.
- the hydrogel of this embodiment has a structure in which a neutralized salt of an ⁇ -olefin-maleic acid copolymer obtained by copolymerizing an ⁇ -olefin and maleic acid as described above is crosslinked with a crosslinking agent such as a polyamine.
- the hydrogel has a transmittance of 40 to 85% in a visible light region (400 to 800 nm) of a 10% by weight aqueous solution.
- the 10 wt% aqueous solution means that the solid content of the binder composition forming the hydrogel is 10 wt% as a solid content not containing water.
- the hydrogel refers to a structure in which a solvent containing water as a main component is taken in and held in a network structure formed by crosslinking a polymer.
- the amount of the solvent contained in the hydrogel of the present embodiment is not particularly limited as long as the transmittance is in the above range.
- the solvent taken into the network structure may contain a solvent that dissolves in water or a solvent that is miscible with water to the extent that the effects of the present invention are not affected.
- the network structure means a network structure stretched in three dimensions by cross-linking an ⁇ -olefin-maleic acid copolymer obtained by copolymerizing ⁇ -olefins and maleic acids. To do. Thereby, flexibility can be given to the hydrogel.
- the hydrogel of the present embodiment preferably has a 10% by weight aqueous solution having a transmittance in the visible light region (400 to 800 nm) of 40 to 85%, more preferably 50 to 75%. More preferably, it is in the range of 45 to 70%.
- the transmittance specifically refers to the transmittance in the visible light region of 400 to 800 nm when measured with a 10 mm cell using, for example, an ultraviolet / visible spectrophotometer.
- the transmittance is higher than 85%, the network structure is not sufficiently formed and a hydrogel cannot be formed. Further, when the transmittance is higher than 85%, the degree of crosslinking is low and the network structure is not developed, so the polymer chain does not spread in the electrode surface, and the particles in the mixed layer cannot be spatially determined. As a result, the flexibility of the electrode is reduced.
- the transmittance is lower than 40%, the crosslinking proceeds too much to increase the viscosity and the productivity is extremely deteriorated, which is not preferable. Also, if the transmittance is too low, the network structure will develop too much, and it will not be able to be sufficiently disintegrated with the solid content at the time of slurry production, and the binder (hydrogel as binder) will not disperse. ⁇ Deterioration of flexibility occurs, causing deterioration of battery characteristics.
- the transmittance in the visible light region (400 to 800 nm) of a 10% by weight aqueous solution is in the range of 40 to 85%, which means that among ⁇ -olefin-maleic acid copolymers.
- the Japanese salt has an appropriate network structure by being appropriately crosslinked.
- the permeability of the hydrogel refers to the type of crosslinking agent (for example, polyamines) described later, the molecular weight, the added amount, and the neutralization degree of the neutralized salt of the ⁇ -olefin-maleic acid copolymer. It can be adjusted by means such as adjustment.
- the method for obtaining the hydrogel of the present embodiment is not particularly limited.
- a neutralized salt of an ⁇ -olefin-maleic acid copolymer as described above is mixed with a crosslinking agent as described above. After the dropwise addition, it can be produced by heating and stirring at about 60 to 90 ° C. for 1 to 8 hours. That is, it can be obtained by using the binder composition of the present embodiment as a raw material and, for example, heating and stirring it as described above.
- the hydrogel of the present embodiment defines the transmittance when the solid content is 10% by weight aqueous solution (that is, when the amount of water is 90% by weight), but is included in the hydrogel of the present embodiment.
- the amount of water is not limited to 90% by weight as long as the effect of the present invention is exhibited.
- the amount of water contained in the hydrogel is preferably 3% to 20% by weight, more preferably 5% to 15% by weight.
- the binder composition that is the raw material of the hydrogel of the present embodiment preferably has the same range viscosity as the above-described binder composition of the present embodiment as the viscosity before heating for producing the hydrogel, and further It is desirable that the viscosity of the 10% by weight aqueous solution before heating at 25 ° C. and at a shear rate of 40 s-1 is 2300 mPa ⁇ s to 15000 mPa ⁇ s.
- the viscosity is too low, the network structure is not sufficiently formed and a hydrogel cannot be formed. If the viscosity is too high, the slurry cannot be sufficiently kneaded, resulting in an unstable slurry as well as difficult electrode formation, leading to an increase in electrical resistance.
- the viscosity in this embodiment can be measured by, for example, a rotational viscometer method.
- the binder composition for nonaqueous electrolyte battery electrodes is often used for production of a slurry composition that continues in a state of containing water. Under the present circumstances, in the said binder composition for nonaqueous electrolyte battery electrodes, you may dilute with water from a viewpoint on viscosity adjustment and manufacture, and you may crush hydrogel. In addition, the hydrogel of this embodiment may be used by further diluting with a solvent such as water in the subsequent production of the slurry composition, or the hydrogel itself may be crushed for viscosity adjustment.
- the method for diluting or crushing the crosslinked binder composition or hydrogel in the present embodiment is not particularly limited as long as a uniform aqueous binder composition solution can be obtained.
- examples thereof include a method using a rotation / revolution mixer, a planetary mixer, a planetary ball mill, a bead mill, and the like.
- the binder composition for a nonaqueous electrolyte battery electrode of the present embodiment is usually a slurry composition for a nonaqueous electrolyte battery electrode (hereinafter simply referred to as a slurry) which further contains an active material and water in addition to the binder composition described above. It is preferably used as a composition). Moreover, it is preferable that the hydrogel of this embodiment is used as a slurry composition for non-aqueous electrolyte battery electrodes further containing an active material. The slurry composition containing the hydrogel may be additionally added with water when it is produced.
- the nonaqueous electrolyte battery negative electrode is characterized in that a current collector is bound with a mixed layer containing at least the binder composition (or hydrogel) of the present embodiment and an active material.
- This negative electrode can be formed by applying the slurry composition described above to a current collector and then removing the solvent by a method such as drying. If necessary, a thickener, a conductive aid and the like can be added to the mixed layer.
- the amount of neutralized salt of ⁇ -olefin-maleic acid copolymer used relative to 100 parts by weight of the active material is usually 0.4 to 15 parts by weight.
- the amount is preferably 0.6 to 10 parts by weight, more preferably 1 to 8 parts by weight. If the amount of the copolymer is too small, the viscosity of the slurry may be too low and the thickness of the mixed layer may be reduced. Conversely, if the amount of the copolymer is excessive, the discharge capacity may be reduced.
- the amount of water in the slurry composition is usually preferably 40 to 150 parts by weight, more preferably 70 to 130 parts by weight with respect to 100 parts by weight of the active material.
- the solvent in the negative electrode slurry composition of the present embodiment in addition to the above water, for example, alcohols such as methanol, ethanol, propanol and 2-propanol, cyclic ethers such as tetrahydrofuran and 1,4-dioxane, N, Amides such as N-dimethylformamide and N, N-dimethylacetamide, cyclic amides such as N-methylpyrrolidone and N-ethylpyrrolidone, and sulfoxides such as dimethylsulfoxide can also be used. In these, use of water is preferable from a viewpoint of safety.
- organic solvents may be used in combination within a range of preferably 20% by weight or less of the total solvent.
- organic solvent preferably has a boiling point at normal pressure of 100 ° C. or higher and 300 ° C. or lower, for example, hydrocarbons such as n-dodecane; alcohols such as 2-ethyl-1-hexanol and 1-nonanol.
- Esters such as ⁇ -butyrolactone and methyl lactate; amides such as N-methylpyrrolidone, N, N-dimethylacetamide and dimethylformamide; and organic dispersion media such as sulfoxides and sulfones such as dimethyl sulfoxide and sulfolane.
- examples of the active material (negative electrode active material) added to the negative electrode slurry composition include amorphous carbon, graphite, natural graphite, and mesocarbon microbeads (MCMB). ), Carbonaceous materials such as pitch-based carbon fibers; conductive polymers such as polyacene; composite metal oxides represented by SiOx, SnOx, LiTiOx, other metal oxides, lithium metals such as lithium metals and lithium alloys A metal compound such as TiS 2 and LiTiS 2 is exemplified.
- a thickener can be further added to the slurry composition as necessary.
- the thickener that can be added is not particularly limited, and various alcohols, in particular, polyvinyl alcohol and modified products thereof, celluloses, starches, and other polysaccharides can be used.
- examples of the conductive auxiliary compounded in the slurry composition as necessary include metal powder, conductive polymer, acetylene black, and the like.
- the amount of the conductive aid used is usually preferably 0.1 to 10 parts by weight, more preferably 0.8 to 7 parts by weight with respect to 100 parts by weight of the negative electrode active material.
- the current collector used for the nonaqueous electrolyte battery negative electrode of the present embodiment is not particularly limited as long as it is made of a conductive material.
- a conductive material For example, iron, copper, aluminum, nickel, stainless steel, titanium, tantalum, gold Metal materials such as platinum can be used. One of these may be used alone, or two or more of these may be used in combination at any ratio.
- the shape of the current collector is not particularly limited, but usually it is preferably a sheet having a thickness of about 0.001 to 0.5 mm.
- the method for applying the slurry to the current collector is not particularly limited. Examples thereof include a doctor blade method, a dip method, a reverse roll method, a direct roll method, a gravure method, an extrusion method, a dipping method, and a brush coating method.
- the amount to be applied is not particularly limited, but the thickness of the mixed layer containing the active material, conductive additive, binder and thickener formed after removing the solvent or dispersion medium by a method such as drying is preferably 0.005 to An amount of 5 mm, more preferably 0.01 to 2 mm is common.
- the method for drying a solvent such as water contained in the slurry composition is not particularly limited, and examples thereof include aeration drying with hot air, hot air, and low-humidity air; vacuum drying; .
- the drying conditions are preferably adjusted so that the solvent can be removed as soon as possible while the active material layer is cracked by stress concentration or the active material layer does not peel from the current collector.
- the pressing method include a die press and a roll press.
- the present invention also includes a non-aqueous electrolyte battery having the negative electrode.
- the nonaqueous electrolyte battery usually includes the negative electrode, the positive electrode, and an electrolytic solution.
- the positive electrode normally used for nonaqueous electrolyte batteries is especially used for a positive electrode without a restriction
- the positive electrode active material TiS 2 , TiS 3 , amorphous MoS 3 , Cu 2 V 2 O 3 , amorphous V 2 O—P 2 O 5 , MoO 3 , V 2 O 5 , V 6 O Transition metal oxides such as 13 and lithium-containing composite metal oxides such as LiCoO 2 , LiNiO 2 , LiMnO 2 , and LiMn 2 O 4 are used.
- the positive electrode active material is made of a conductive additive similar to that of the negative electrode, and a binder such as SBR, NBR, acrylic rubber, hydroxyethyl cellulose, carboxymethyl cellulose, polyvinylidene fluoride, and the boiling point at 100 ° C. in water or the above normal pressure.
- a binder such as SBR, NBR, acrylic rubber, hydroxyethyl cellulose, carboxymethyl cellulose, polyvinylidene fluoride, and the boiling point at 100 ° C. in water or the above normal pressure.
- the positive electrode slurry prepared by mixing in a solvent of 300 ° C. or lower can be applied to a positive electrode current collector such as aluminum and the solvent can be dried to obtain a positive electrode.
- an electrolytic solution in which an electrolyte is dissolved in a solvent can be used.
- the electrolyte solution may be liquid or gel as long as it is used for a non-aqueous electrolyte battery such as a normal lithium ion secondary battery, and functions as a battery depending on the type of the negative electrode active material and the positive electrode active material. What is necessary is just to select suitably.
- lithium salt for example, also known lithium salt is any conventionally available, LiClO 4, LiBF 6, LiPF 6, LiCF 3 SO 3, LiCF 3 CO 2, LiAsF 6, LiSbF 6, LiB 10 Cl 10 , LiAlC l4, LiCl, LiBr, LiB (C 2 H 5) 4, CF 3 SO 3 Li, CH 3 SO 3 Li, LiCF 3 SO 3, LiC 4 F 9 SO 3, Li (CF 3 SO 2) 2 N And lower aliphatic lithium carboxylates.
- the solvent for dissolving such an electrolyte is not particularly limited. Specific examples include carbonates such as propylene carbonate, ethylene carbonate, butylene carbonate, dimethyl carbonate, and diethyl carbonate; lactones such as ⁇ -butyllactone; trimethoxymethane, 1,2-dimethoxyethane, diethyl ether, and 2-ethoxyethane.
- Ethers such as tetrahydrofuran, 2-methyltetrahydrofuran; sulfoxides such as dimethyl sulfoxide; oxolanes such as 1,3-dioxolane, 4-methyl-1,3-dioxolane; nitrogen-containing compounds such as acetonitrile and nitromethane; formic acid Organic acid esters such as methyl, methyl acetate, ethyl acetate, butyl acetate, methyl propionate and ethyl propionate; inorganic acid esters such as triethyl phosphate, dimethyl carbonate and diethyl carbonate Tergories; diglymes; triglymes; sulfolanes; oxazolidinones such as 3-methyl-2-oxazolidinone; sultones such as 1,3-propane sultone, 1,4-butane sultone, naphtha sultone, and the like.
- a gel electrolyte a nitrile polymer, an acrylic polymer, a fluorine polymer, an alkylene oxide polymer, or the like can be added as a gelling agent.
- the method for producing the non-aqueous electrolyte battery of the present embodiment is not particularly limited, and for example, the following production method is exemplified. That is, the negative electrode and the positive electrode are overlapped with each other via a separator such as a polypropylene porous membrane, wound or folded according to the shape of the battery, put into a battery container, injected with an electrolyte, and sealed.
- the shape of the battery may be any known coin type, button type, sheet type, cylindrical type, square type, flat type, and the like.
- the nonaqueous electrolyte battery of the present embodiment is a battery that achieves both improved adhesion and improved battery characteristics, and is useful for various applications. For example, it is very useful as a battery for portable terminals that require miniaturization (light weight, thinning, etc.) and high performance (high output, high capacity, low resistance, long life, etc.). It is.
- the binder composition for a nonaqueous electrolyte battery electrode according to one aspect of the present invention (hereinafter also simply referred to as a binder composition) is an ⁇ -olefin-maleic acid copolymer obtained by copolymerizing an ⁇ -olefin and a maleic acid.
- a binder composition for a non-aqueous electrolyte battery electrode having a structure in which a neutralized salt of a coalescence is cross-linked with polyamines, and a viscosity of an aqueous solution containing 10% by weight of the binder composition at 25 ° C. and a shear rate of 40 s ⁇ 1 Is 1800 mPa ⁇ s to 15000 mPa ⁇ s.
- the battery characteristics can be improved without impairing the binding property between the active materials and the collector electrode and the toughness as the electrode.
- a hydrogel having a transmittance of 40 to 85% in a visible light region (400 to 800 nm) of a 10% by weight aqueous solution obtained from the binder composition is preferable.
- a three-dimensional network structure is developed with the above-described configuration, and a transparent hydrogel can be provided.
- battery characteristics low resistance
- functionality A hydrogel excellent in flexibility
- the hydrogel of the present invention has an advantage that it can be obtained by a relatively simple production method.
- a slurry composition for a nonaqueous electrolyte battery electrode is characterized by containing the binder composition and an active material.
- a slurry composition for a nonaqueous electrolyte battery electrode according to still another aspect of the present invention is characterized by containing the hydrogel and an active material.
- a non-aqueous electrolyte battery negative electrode is formed by binding a current collector to a mixed layer containing at least the binder composition for a non-aqueous electrolyte battery electrode and an active material.
- a nonaqueous electrolyte battery negative electrode is characterized in that a mixed layer containing at least the hydrogel and an active material is bound to a current collector.
- a nonaqueous electrolyte battery according to still another aspect of the present invention is characterized by having the above nonaqueous electrolyte battery negative electrode.
- Example 1 ⁇ Preparation of binder composition> Using a water-soluble lithium-modified isobutene-maleic anhydride copolymer resin (average molecular weight 325,000, neutralization degree 0.5, ring-opening rate 96%), a 10% by weight aqueous solution was prepared and used in the following tests. . The pH is adjusted by adjusting the degree of neutralization of the copolymer resin. Specifically, 1 equivalent (0.16 mol) of lithium hydroxide is added to the maleic acid unit in the maleic acid copolymer. Went by.
- the slurry for the electrode was prepared by using 6.452 parts by weight of a 5% by weight aqueous solution of the binder composition for the negative electrode as a solid content with respect to 100 parts by weight of natural graphite (DMGS, manufactured by BYD) as the negative electrode active material, and a conductive auxiliary agent ( Super-P (made by Timcal Co., Ltd.) as a conductivity imparting agent) 1.075 parts by weight as a solid content is put into a special container and kneaded using a planetary stirrer (ARE-250, made by Shinky) for electrode coating.
- a slurry was prepared.
- Electrode toughness test Evaluation of electrode toughness is based on JIS K5600-5-1 (General coating test method-Part 5: Mechanical properties of coating film-Section 1: Bending resistance (cylindrical mandrel method)) Used. When the electrode crack was visually confirmed, no crack was observed even at the minimum diameter of 2 mm in this test. Therefore, 1.5 mm, 1.0 mm, 0.8 mm, and 0.5 mm SUS bars (manufactured by SUS304Wire Nilaco) were prepared, and an electrode winding test was performed. Table 1 below shows the results of the minimum SUS diameter in which no cracks occurred.
- the battery coated electrode (battery negative electrode) obtained above was transferred to a glove box (manufactured by Miwa Seisakusho) under an argon gas atmosphere.
- a metal lithium foil (thickness 0.2 mm, ⁇ 16 mm) was used for the positive electrode.
- ⁇ Evaluation method charge / discharge characteristic test>
- the produced coin battery was subjected to a charge / discharge test using a commercially available charge / discharge tester (TOSCAT3100, manufactured by Toyo System).
- the coin battery is placed in a constant temperature bath at 25 ° C., and charging is performed with a constant current of 0.1 C (about 0.5 mA / cm 2 ) with respect to the amount of active material until the voltage reaches 0 V with respect to the lithium potential.
- the constant voltage charge of 0V was implemented to the electric current of 0.02 mA.
- the capacity at this time was defined as a charging capacity (mAh / g).
- the binder composition was prepared by The viscosity results at a shear rate of 40 s -1 are shown in Table 1 below.
- the electrode slurry preparation is 6.452 parts by weight of a 10% by weight aqueous solution of the binder composition for the negative electrode as a solid content with respect to 100 parts by weight of natural graphite (DMGS, manufactured by BYD) as the negative electrode active material, and a conductive additive ( Super-P (made by Timcal Co., Ltd.) as a conductivity imparting agent) 1.075 parts by weight as a solid content is put into a special container and kneaded using a planetary stirrer (ARE-250, made by Shinky) for electrode coating.
- a slurry (slurry for negative electrode) was prepared.
- a coated negative electrode (a negative electrode for a battery) was prepared in the same manner as in Example 1 to obtain a coin battery, and a charge / discharge characteristic test was performed. In addition, a toughness test and a peel strength measurement were performed using a coated electrode (peel strength, electrode for toughness test). The results are shown in Table 1 below.
- Example 4 A 10% by weight aqueous solution of a water-soluble lithium-modified isobutene-maleic anhydride copolymer resin (average molecular weight 325,000, neutralization degree 0.7, ring opening rate 97%) was prepared, and lithium hydroxide was co-polymerized with maleic acids. The pH was adjusted by adding 1.4 equivalents to the maleic acid unit in the coalescence.
- the viscosity results at a shear rate of 40 s -1 are shown in Table 1 below.
- a slurry for a nonaqueous electrolyte battery electrode was produced in the same manner as in Example 2 above.
- a coated negative electrode was prepared by the same method as in Example 1 to obtain a coin battery, and a charge / discharge characteristic test was performed. Moreover, the toughness test and peel strength measurement were performed using the coated electrode. The results are shown in Table 1 below.
- Example 5 A 10% by weight aqueous solution of a water-soluble lithium-modified isobutene-maleic anhydride copolymer resin (average molecular weight 325,000, neutralization degree 0.4, ring opening rate 92%) was prepared, and lithium hydroxide was co-polymerized with maleic acids. The pH was adjusted by adding 0.8 equivalent to the maleic acid unit in the coalescence.
- the viscosity results at a shear rate of 40 s -1 are shown in Table 1 below.
- the binder composition was diluted by the same method as in Example 1 to obtain a 5% by weight binder composition.
- a slurry for a nonaqueous electrolyte battery electrode was produced by the same method as in Example 1 above.
- a coated negative electrode was prepared by the same method as in Example 1 to obtain a coin battery, and a charge / discharge characteristic test was performed.
- the toughness test and peel strength measurement were performed using the coated electrode. The results are shown in Table 1 below.
- Example 1 A 10% by weight aqueous solution of the resin used in Example 1 was prepared and used as a negative electrode binder composition without adding PEI. The viscosity results at a shear rate of 40 s -1 are shown in Table 1 below.
- a slurry for a nonaqueous electrolyte battery electrode was produced in the same manner as in Example 2 above. Further, a coated negative electrode was prepared by the same method as in Example 1 to obtain a coin battery, and a charge / discharge characteristic test was performed. Moreover, the toughness test and peel strength measurement were performed using the coated electrode. The results are shown in Table 1 below.
- the binder composition was prepared by The viscosity results at a shear rate of 40 s -1 are shown in Table 1 below. Thereafter, a slurry for a nonaqueous electrolyte battery electrode was produced in the same manner as in Example 2 above. Further, a coated negative electrode was prepared by the same method as in Example 1 to obtain a coin battery, and a charge / discharge characteristic test was performed. Moreover, the toughness test and peel strength measurement were performed using the coated electrode. The results are shown in Table 1 below.
- the crosslinking agent (polyamines) is contained in the negative electrode binder composition, and the viscosity at 25 ° C. and the shear rate of 40 s ⁇ 1 of the aqueous solution containing 10% by weight is 1800 mPa ⁇ s to 12000 mPa ⁇ s. Improvement of toughness and adhesiveness was observed due to the crosslinking effect caused by the formation of acid and salt. In addition, since the viscosity is increased by adding a crosslinking agent, it is possible to prepare a slurry without using a thickener. As is apparent from Table 1, it was shown that the addition of a cross-linking agent does not significantly affect the battery characteristics and realizes low resistance. In contrast, Comparative Example 1 that does not contain polyamines and Comparative Examples 2 to 4 in which the viscosity is outside the scope of the present invention even when polyamines are added resulted in low toughness and adhesion. .
- Example 6 (Example 6) ⁇ Manufacture of hydrogel> A water-soluble lithium-modified isobutene-maleic anhydride copolymer resin (average molecular weight 325,000, neutralization degree 0.5, ring-opening rate 96%) was used, and a 10% by weight aqueous solution was prepared and used in the following tests. .
- a 10% by weight aqueous solution of polyethyleneimine (PEI, average molecular weight 10,000, manufactured by Nippon Shokubai Co., Ltd.) as a cross-linking agent was added to the 10% by weight aqueous resin solution. Then, it was dropped at 2.0 ml / h while stirring with a hand mixer (WARING STAND MIXER, manufactured by WARING). Thereafter, the mixture was heated and stirred at 90 ° C. for 2 hours to obtain a hydrogel.
- PEI polyethyleneimine
- ⁇ Dilution of hydrogel> An equivalent amount of water was added to 10% by weight of the hydrogel prepared above, and 5% by weight of a negative electrode binder liquid was obtained using a hand mixer (WARING STAND MIXER, manufactured by WARING).
- slurry for electrode coating was prepared in the same manner as in Test Example 1 (Example 1) except that a 5 wt% aqueous solution of hydrogel was used instead of the 5 wt% aqueous solution of the negative electrode binder composition.
- Example 8 A 10% by weight aqueous solution of a water-soluble lithium-modified isobutene-maleic anhydride copolymer resin (average molecular weight 325,000, neutralization degree 0.7, ring opening rate 97%) was prepared.
- Example 9 A 10% by weight aqueous solution of a water-soluble lithium-modified isobutene-maleic anhydride copolymer resin (average molecular weight 325,000, neutralization degree 0.4, ring opening rate 92%) was prepared.
- Example 11 As a negative electrode binder composition, a 10% by weight aqueous solution of a water-soluble lithium-modified methyl vinyl ether-maleic anhydride copolymer resin (average molecular weight 630,000, neutralization degree 0.5, ring opening rate 96%) was prepared.
- Example 12 A 10% by weight aqueous solution of a water-soluble lithium-modified ethylene-maleic anhydride copolymer resin (average molecular weight 350,000, neutralization degree 0.5, ring opening rate 96%) was prepared.
- Example 6 Using the resin and crosslinking agent (PEI, molecular weight 600) used in Example 7, a hydrogel was prepared by the same method as in Example 7, and the transmittance and viscosity were measured. The results are shown in Table 2 below. Thereafter, a hydrogel dilution and a nonaqueous electrolyte battery slurry were prepared in the same manner as in Example 6. Further, a coated negative electrode was prepared by the same method as in Example 6 to obtain a coin battery, and a charge / discharge characteristic test was performed. Moreover, the flexibility test was done using the coated electrode. The results are shown in Table 2 below.
- Example 7 The results of measuring the transmittance and viscosity of a 10% by weight aqueous resin solution (no additive) used in Example 6 are shown in Table 2 below. Thereafter, a slurry for a non-aqueous electrolyte battery was produced in the same manner as in Example 6 using the 10 wt% aqueous solution as a binder solution. Further, a coated negative electrode was prepared by the same method as in Example 6 to obtain a coin battery, and a charge / discharge characteristic test was performed. Moreover, the flexibility test was done using the coated electrode. The results are shown in Table 2 below.
- Example 8 Table 2 below shows the results of measuring the transmittance and viscosity of a 10% by weight aqueous solution (without additives) of the resin used in Example 10. Then, the slurry for nonaqueous electrolyte batteries was produced by the method similar to the said comparative example 7. Subsequently, the coating negative electrode was produced by the method similar to the said Example 6, the coin battery was obtained, and the charge / discharge characteristic test was done. Moreover, the flexibility test was done using the coated electrode. The results are shown in Table 2 below.
- Example 9 The results of measuring the viscosity and transmittance of a 10% by weight aqueous solution of the resin used in Example 11 (without additives) are shown in Table 2 below. Then, the slurry for nonaqueous electrolyte batteries was produced by the method similar to the said comparative example 7. Further, a coated negative electrode was prepared by the same method as in Example 6 to obtain a coin battery, and a charge / discharge characteristic test was performed. Moreover, the flexibility test was done using the coated electrode. The results are shown in Table 2 below.
- aqueous SBR emulsion aqueous solution (TRD2001, 48.3% by weight), which is a conventional aqueous negative electrode binder composition, and CMC-Na (cellogen BSH-6, 10% by weight) as a thickener.
- a slurry for a nonaqueous electrolyte battery was prepared by the method.
- a coated negative electrode was prepared by the same method as in Example 6 to obtain a coin battery, and a charge / discharge characteristic test was performed. Moreover, the flexibility test was done using the coated electrode. The results are shown in Table 2 below.
- Comparative Example 5 in which the addition amount of the cross-linking agent was high and the transmittance was low, the viscosity was too high, and crushing at the time of slurry preparation could not be sufficiently performed, resulting in a battery having high resistance. Furthermore, in Comparative Example 6 in which the molecular weight of the polyamines was low, the degree of crosslinking was not sufficient, so the viscosity was low, and sufficient flexibility could not be provided.
- the present invention has wide industrial applicability in the technical field related to non-aqueous electrolyte batteries such as lithium ion secondary batteries.
Abstract
Description
現在、一般に知られているハイドロゲルを形成するものとしては、例えば、澱粉、カラギーナン、繊維素誘導体、ゼラチン、カゼイン、ポリビニルアルコール、ポリビニルピロリドン、ポリアクリル酸、ポリオキシエチレンオキサイド等の水溶性重合体がある。これらの水溶性重合体を用いるハイドロゲルは保香材、防火材、保温材、保冷材等の用途に広く利用されている。 Furthermore, it is preferable that the binder composition of this embodiment is a hydrogel.
Examples of water gels that are currently known to form hydrogels include water-soluble polymers such as starch, carrageenan, fiber derivatives, gelatin, casein, polyvinyl alcohol, polyvinyl pyrrolidone, polyacrylic acid, and polyoxyethylene oxide. There is. Hydrogels using these water-soluble polymers are widely used in applications such as a fragrance material, a fireproof material, a heat insulation material, and a cold insulation material.
(実施例1)
<バインダー組成物の調製>
水溶性のリチウム変性イソブテン-無水マレイン酸共重合樹脂(平均分子量325,000、中和度0.5、開環率96%)を用い、10重量%水溶液を調製して以下の試験で用いた。pHの調整は、共重合樹脂の中和度を調整することで行い、具体的には、水酸化リチウムをマレイン酸類共重合体中のマレイン酸単位に対し1当量(0.16mol)添加することによって行った。 <Test Example 1>
Example 1
<Preparation of binder composition>
Using a water-soluble lithium-modified isobutene-maleic anhydride copolymer resin (average molecular weight 325,000, neutralization degree 0.5, ring-opening rate 96%), a 10% by weight aqueous solution was prepared and used in the following tests. . The pH is adjusted by adjusting the degree of neutralization of the copolymer resin. Specifically, 1 equivalent (0.16 mol) of lithium hydroxide is added to the maleic acid unit in the maleic acid copolymer. Went by.
Brookfield型粘度計(DV-I PRIMEブルックフィールド社製)を用いて25℃で、上記で得られたバインダー組成物10重量%水溶液(バインダー水溶液)の粘度の測定を行った。ずり速度40s-1の時の粘度結果を下記表1に示す。 <Measurement of viscosity of binder composition for negative electrode>
Using a Brookfield viscometer (DV-I PRIME Brookfield), the viscosity of the 10% by weight aqueous solution (binder aqueous solution) of the binder composition obtained above was measured at 25 ° C. The viscosity results when the shear rate 40 s -1 are shown in Table 1 below.
上記で作製した10重量%のバインダー液(バインダー水溶液)に当量の水を加え、遊星攪拌器(ARE-250、シンキー製)を用いて希釈を行い、5重量%のバインダー組成物を得た。 <Dilution of binder liquid>
An equivalent amount of water was added to the 10% by weight of the binder solution (binder aqueous solution) prepared above, and diluted using a planetary stirrer (ARE-250, manufactured by Sinky) to obtain a 5% by weight binder composition.
電極用スラリー作製は負極用活物質として天然黒鉛(DMGS、BYD製)100重量部に対して、負極用バインダー組成物の5重量%水溶液を固形分として6.452重量部、および導電助剤(導電付与剤)としてSuper-P(ティムカル社製)を固形分として1.075重量部を専用容器に投入し、遊星攪拌器(ARE-250、シンキー製)を用いて混練し、電極塗工用スラリーを作製した。スラリー中の活物質とバインダーの組成比は固形分として、黒鉛粉末:導電助剤:バインダー組成物=100:1.075:6.452である。 <Preparation of slurry for negative electrode>
The slurry for the electrode was prepared by using 6.452 parts by weight of a 5% by weight aqueous solution of the binder composition for the negative electrode as a solid content with respect to 100 parts by weight of natural graphite (DMGS, manufactured by BYD) as the negative electrode active material, and a conductive auxiliary agent ( Super-P (made by Timcal Co., Ltd.) as a conductivity imparting agent) 1.075 parts by weight as a solid content is put into a special container and kneaded using a planetary stirrer (ARE-250, made by Shinky) for electrode coating. A slurry was prepared. The composition ratio of the active material and the binder in the slurry is, as a solid content, graphite powder: conducting aid: binder composition = 100: 1.075: 6.452.
得られたスラリーを、バーコーター(T101、松尾産業製)を用いて集電体の銅箔(CST8G、福田金属箔粉工業製)上に塗工し、室温(24.5℃)で一次乾燥後、ロールプレス(宝泉製)を用いて圧延処理を行なった。その後、電池用電極(φ14mm)として打ち抜き後、140℃で3時間減圧条件の二次乾燥によってコイン電池用電極(電池用負極)を作製した。 <Preparation of negative electrode for battery>
The obtained slurry was coated on a current collector copper foil (CST8G, manufactured by Fukuda Metal Foil Co., Ltd.) using a bar coater (T101, manufactured by Matsuo Sangyo), and then primary dried at room temperature (24.5 ° C). Then, the rolling process was performed using the roll press (made by Hosen). Then, after punching out as a battery electrode (φ14 mm), a coin battery electrode (battery negative electrode) was produced by secondary drying under reduced pressure conditions at 140 ° C. for 3 hours.
得られたスラリーを、バーコーター(T101、松尾産業製)を用いて集電体の銅箔(CST8G、福田金属箔粉工業製)上に塗工し、室温(24.5℃)で一次乾燥後、ロールプレス(宝泉製)を用いて圧延処理を行なった電極(膜厚約50μm)を用いて試験を行った。 <Preparation of peel strength and toughness test electrode>
The obtained slurry was coated on a current collector copper foil (CST8G, manufactured by Fukuda Metal Foil Co., Ltd.) using a bar coater (T101, manufactured by Matsuo Sangyo), and then primary dried at room temperature (24.5 ° C). Then, it tested using the electrode (film thickness of about 50 micrometers) which performed the rolling process using the roll press (made by Hosen).
電極の靭性の評価はJIS K5600-5-1(塗料一般試験方法-第5部:塗膜の機械的性質-第1節:耐屈曲性(円筒形マンドレル法))のタイプ1の試験装置を用いて行った。電極割れの確認を目視で行ったところ、本試験での最小径2mmでも割れが生じなかった。そこで、1.5mm、1.0mm、0.8mm、0.5mmのSUS棒(SUS304Wire ニラコ製)を用意し、電極巻き付け試験を行った。割れが生じなかった最小のSUS径の結果を下記表1に示す。 <Electrode toughness test>
Evaluation of electrode toughness is based on JIS K5600-5-1 (General coating test method-Part 5: Mechanical properties of coating film-Section 1: Bending resistance (cylindrical mandrel method)) Used. When the electrode crack was visually confirmed, no crack was observed even at the minimum diameter of 2 mm in this test. Therefore, 1.5 mm, 1.0 mm, 0.8 mm, and 0.5 mm SUS bars (manufactured by SUS304Wire Nilaco) were prepared, and an electrode winding test was performed. Table 1 below shows the results of the minimum SUS diameter in which no cracks occurred.
集電極である銅箔から電極を剥離したときの強度を測定した。当該剥離強度は、50Nのロードセル(株式会社イマダ製)を用いて180°剥離強度を測定した。上記で得られた電池用塗工電極のスラリー塗布面とステンレス板とを両面テープ(ニチバン製両面テープ)を用いて貼り合わせ、180°剥離強度(剥離幅10mm、剥離速度100mm/min)を測定した。上記結果を下記表1に示す。 <Measurement of peel strength of electrode>
The strength when the electrode was peeled off from the copper foil as the collecting electrode was measured. The peel strength was measured at 180 ° peel strength using a 50N load cell (manufactured by Imada Co., Ltd.). The slurry-coated surface of the battery-coated electrode obtained above and a stainless steel plate were bonded together using a double-sided tape (double-faced tape made by Nichiban), and the 180 ° peel strength (peel width 10 mm, peel rate 100 mm / min) was measured. did. The results are shown in Table 1 below.
上記で得られた電池用塗工電極(電池用負極)をアルゴンガス雰囲気下のグローブボックス(美和製作所製)に移送した。正極には金属リチウム箔(厚さ0.2mm、φ16mm)を用いた。また、セパレーターとしてポリプロピレン系(セルガード#2400、ポリポア製)を使用して、電解液は六フッ化リン酸リチウム(LiPF6)のエチレンカーボネート(EC)とエチルメチルカーボネート(EMC)にビニレンカーボネート(VC)を添加した混合溶媒系(1M-LiPF6、EC/EMC=3/7vol%、VC2重量%)を用いて注入し、コイン電池(2032タイプ)を作製した。 <Production of battery>
The battery coated electrode (battery negative electrode) obtained above was transferred to a glove box (manufactured by Miwa Seisakusho) under an argon gas atmosphere. A metal lithium foil (thickness 0.2 mm, φ16 mm) was used for the positive electrode. In addition, a polypropylene system (Celgard # 2400, manufactured by Polypore) is used as a separator, and the electrolyte is ethylene carbonate (EC) of lithium hexafluorophosphate (LiPF 6 ) and ethylene carbonate (EMC) with vinylene carbonate (VC). ) added was mixed solvent system (1M-LiPF 6, EC / EMC = 3 / 7vol%, were injected with VC2 wt%) to prepare a coin battery (2032 type).
作製したコイン電池は、市販充放電試験機(TOSCAT3100、東洋システム製)を用いて充放電試験を実施した。コイン電池を25℃の恒温槽に置き、充電はリチウム電位に対して0Vになるまで活物質量に対して0.1C(約0.5mA/cm2)の定電流充電を行い、更にリチウム電位に対して0.02mAの電流まで0Vの定電圧充電を実施した。このときの容量を充電容量(mAh/g)とした。次いで、リチウム電位に対して0.1C(約0.5mA/cm2)の定電流放電を1.5Vまで行い、このときの容量を放電容量(mAh/g)とした。初期放電容量と充電容量差を不可逆容量、放電容量/充電容量の百分率を充放電効率とした。コイン電池の直流抵抗は、1回の充電を行った後(満充電状態)の抵抗値を採用した。上記結果を下記表1に示す。 <Evaluation method: charge / discharge characteristic test>
The produced coin battery was subjected to a charge / discharge test using a commercially available charge / discharge tester (TOSCAT3100, manufactured by Toyo System). The coin battery is placed in a constant temperature bath at 25 ° C., and charging is performed with a constant current of 0.1 C (about 0.5 mA / cm 2 ) with respect to the amount of active material until the voltage reaches 0 V with respect to the lithium potential. On the other hand, the constant voltage charge of 0V was implemented to the electric current of 0.02 mA. The capacity at this time was defined as a charging capacity (mAh / g). Next, a constant current discharge of 0.1 C (about 0.5 mA / cm 2 ) was performed up to 1.5 V with respect to the lithium potential, and the capacity at this time was defined as a discharge capacity (mAh / g). The difference between the initial discharge capacity and the charge capacity was taken as the irreversible capacity, and the percentage of the discharge capacity / charge capacity was taken as the charge / discharge efficiency. As the direct current resistance of the coin battery, a resistance value after being charged once (fully charged state) was adopted. The results are shown in Table 1 below.
実施例1で用いた樹脂と架橋剤(PEI)を用いて、樹脂の10重量%水溶液:PEIの10重量%水溶液=99.7:0.3となるように、実施例1と同様の方法によってバインダー組成物の調製を行った。ずり速度40s-1の時の粘度結果を下記表1に示す。 (Example 2)
Using the resin and the crosslinking agent (PEI) used in Example 1, the same method as in Example 1 so that 10% by weight aqueous solution of resin: 10% by weight aqueous solution of PEI = 99.7: 0.3 The binder composition was prepared by The viscosity results at a shear rate of 40 s -1 are shown in Table 1 below.
実施例1で用いた樹脂とPEIを用いて、樹脂の10重量%水溶液:PEIの10重量%水溶液=98:2となるように、実施例1と同様の方法によってバインダー組成物の調製を行った。ずり速度40s-1の時の粘度結果を下記表1に示す。その後、実施例1と同様の方法によってバインダー組成物を希釈し、5重量%のバインダー組成物を得た。次に、非水電解質電池電極用スラリー(負極用スラリー)を上記実施例1と同様の方法によって作製した。さらに、上記実施例1と同様の方法によって塗工負極を作製し、コイン電池を得て、充放電特性試験を行った。また塗工電極を用いて、靱性試験及び剥離強度測定を行った。結果を下記表1に示す。 (Example 3)
Using the resin and PEI used in Example 1, a binder composition was prepared in the same manner as in Example 1 so that the resin was 10% by weight aqueous solution: PEI 10% by weight aqueous solution = 98: 2. It was. The viscosity results at a shear rate of 40 s -1 are shown in Table 1 below. Thereafter, the binder composition was diluted by the same method as in Example 1 to obtain a 5% by weight binder composition. Next, a nonaqueous electrolyte battery electrode slurry (negative electrode slurry) was prepared in the same manner as in Example 1 above. Further, a coated negative electrode was prepared by the same method as in Example 1 to obtain a coin battery, and a charge / discharge characteristic test was performed. Moreover, the toughness test and peel strength measurement were performed using the coated electrode. The results are shown in Table 1 below.
水溶性のリチウム変性イソブテン-無水マレイン酸共重合樹脂(平均分子量325,000、中和度0.7、開環率97%)の10重量%水溶液を調製し、水酸化リチウムをマレイン酸類共重合体中のマレイン酸単位に対し1.4当量添加することによってpHの調整を行った。 Example 4
A 10% by weight aqueous solution of a water-soluble lithium-modified isobutene-maleic anhydride copolymer resin (average molecular weight 325,000, neutralization degree 0.7, ring opening rate 97%) was prepared, and lithium hydroxide was co-polymerized with maleic acids. The pH was adjusted by adding 1.4 equivalents to the maleic acid unit in the coalescence.
水溶性のリチウム変性イソブテン-無水マレイン酸共重合樹脂(平均分子量325,000、中和度0.4、開環率92%)の10重量%水溶液を調製し、水酸化リチウムをマレイン酸類共重合体中のマレイン酸単位に対し0.8当量添加することによってpHの調整を行った。 (Example 5)
A 10% by weight aqueous solution of a water-soluble lithium-modified isobutene-maleic anhydride copolymer resin (average molecular weight 325,000, neutralization degree 0.4, ring opening rate 92%) was prepared, and lithium hydroxide was co-polymerized with maleic acids. The pH was adjusted by adding 0.8 equivalent to the maleic acid unit in the coalescence.
実施例1で用いた樹脂の10重量%水溶液を調製し、PEIを加えることなく、そのまま負極用バインダー組成物として用いた。ずり速度40s-1の時の粘度結果を下記表1に示す。非水電解質電池電極用スラリーを上記実施例2と同様の方法によって作製した。さらに、上記実施例1と同様の方法によって塗工負極を作製し、コイン電池を得て、充放電特性試験を行った。また塗工電極を用いて、靱性試験及び剥離強度測定を行った。結果を下記表1に示す。 (Comparative Example 1)
A 10% by weight aqueous solution of the resin used in Example 1 was prepared and used as a negative electrode binder composition without adding PEI. The viscosity results at a shear rate of 40 s -1 are shown in Table 1 below. A slurry for a nonaqueous electrolyte battery electrode was produced in the same manner as in Example 2 above. Further, a coated negative electrode was prepared by the same method as in Example 1 to obtain a coin battery, and a charge / discharge characteristic test was performed. Moreover, the toughness test and peel strength measurement were performed using the coated electrode. The results are shown in Table 1 below.
実施例1で用いた樹脂と架橋剤(PEI)を用いて、樹脂の10重量%水溶液:PEIの10重量%水溶液=99.97:0.03となるように、実施例1と同様の方法によってバインダー組成物の調製を行った。ずり速度40s-1の時の粘度結果を下記表1に示す。その後非水電解質電池電極用スラリーを上記実施例2と同様の方法によって作製した。さらに、上記実施例1と同様の方法によって塗工負極を作製し、コイン電池を得て、充放電特性試験を行った。また塗工電極を用いて、靱性試験及び剥離強度測定を行った。結果を下記表1に示す。 (Comparative Example 2)
Using the resin and crosslinking agent (PEI) used in Example 1, the same method as in Example 1 so that the 10% by weight aqueous resin solution: 10% by weight aqueous PEI solution = 99.97: 0.03 The binder composition was prepared by The viscosity results at a shear rate of 40 s -1 are shown in Table 1 below. Thereafter, a slurry for a nonaqueous electrolyte battery electrode was produced in the same manner as in Example 2 above. Further, a coated negative electrode was prepared by the same method as in Example 1 to obtain a coin battery, and a charge / discharge characteristic test was performed. Moreover, the toughness test and peel strength measurement were performed using the coated electrode. The results are shown in Table 1 below.
実施例1で用いた樹脂とPEIを用いて、樹脂の10重量%水溶液:PEIの10重量%水溶液=90:10となるように、実施例1と同様の方法によってバインダー組成物の調製を行った。ずり速度40s-1の時の粘度結果を下記表1に示す。その後、実施例1と同様の方法によってバインダー組成物を希釈し、5重量%のバインダー組成物を得た。次に、非水電解質電池電極用スラリーを上記実施例1と同様の方法によって作製した。さらに、上記実施例1と同様の方法によって塗工負極を作製し、コイン電池を得て、充放電特性試験を行った。また塗工電極を用いて、靱性試験及び剥離強度測定を行った。結果を下記表1に示す。 (Comparative Example 3)
Using the resin and PEI used in Example 1, a binder composition was prepared in the same manner as in Example 1 so that the resin was 10 wt% aqueous solution: PEI 10 wt% aqueous solution = 90: 10. It was. The viscosity results at a shear rate of 40 s -1 are shown in Table 1 below. Thereafter, the binder composition was diluted by the same method as in Example 1 to obtain a 5% by weight binder composition. Next, a slurry for a nonaqueous electrolyte battery electrode was produced by the same method as in Example 1 above. Further, a coated negative electrode was prepared by the same method as in Example 1 to obtain a coin battery, and a charge / discharge characteristic test was performed. Moreover, the toughness test and peel strength measurement were performed using the coated electrode. The results are shown in Table 1 below.
実施例1で用いた樹脂とポリアリルアミン(分子量3000)を用いて、樹脂の10重量%水溶液:PEIの10重量%水溶液=99:1となるように、実施例1と同様の方法によってバインダー組成物の調製を行った。ずり速度40s-1の時の粘度結果を下記表1に示す。その後、実施例1と同様の方法によってバインダー組成物を希釈し、5重量%のバインダー組成物を得た。次に、非水電解質電池電極用スラリーを上記実施例1と同様の方法によって作製した。さらに、上記実施例1と同様の方法によって塗工負極を作製し、コイン電池を得て、充放電特性試験を行った。また塗工電極を用いて、靱性試験及び剥離強度測定を行った。結果を下記表1に示す。 (Comparative Example 4)
Using the resin and polyallylamine (molecular weight 3000) used in Example 1, a binder composition was prepared in the same manner as in Example 1 so that the resin 10 wt% aqueous solution: PEI 10 wt% aqueous solution = 99: 1. The product was prepared. The viscosity results at a shear rate of 40 s -1 are shown in Table 1 below. Thereafter, the binder composition was diluted by the same method as in Example 1 to obtain a 5% by weight binder composition. Next, a slurry for a nonaqueous electrolyte battery electrode was produced by the same method as in Example 1 above. Further, a coated negative electrode was prepared by the same method as in Example 1 to obtain a coin battery, and a charge / discharge characteristic test was performed. Moreover, the toughness test and peel strength measurement were performed using the coated electrode. The results are shown in Table 1 below.
負極用バインダー組成物に架橋剤(ポリアミン類)が含まれ、10重量%含有する水溶液の25℃且つずり速度40s-1における粘度が1800mPa・s~12000mPa・sにある実施例1~5では、酸と塩を形成したことによる架橋効果で靭性、接着性の向上が見られた。また、架橋剤を添加することで増粘するため、増粘剤を用いることなくスラリー作製が可能となった。そして、表1から明らかなように、架橋剤を添加しても電池特性には大きく影響を与えず、低抵抗化が実現することが示された。これに対し、ポリアミン類が含有していない比較例1およびポリアミン類を添加しても粘度が本発明の範囲外となる比較例2~4では、靭性、接着性が共に低いという結果となった。 (Discussion)
In Examples 1 to 5, the crosslinking agent (polyamines) is contained in the negative electrode binder composition, and the viscosity at 25 ° C. and the shear rate of 40 s −1 of the aqueous solution containing 10% by weight is 1800 mPa · s to 12000 mPa · s. Improvement of toughness and adhesiveness was observed due to the crosslinking effect caused by the formation of acid and salt. In addition, since the viscosity is increased by adding a crosslinking agent, it is possible to prepare a slurry without using a thickener. As is apparent from Table 1, it was shown that the addition of a cross-linking agent does not significantly affect the battery characteristics and realizes low resistance. In contrast, Comparative Example 1 that does not contain polyamines and Comparative Examples 2 to 4 in which the viscosity is outside the scope of the present invention even when polyamines are added resulted in low toughness and adhesion. .
(実施例6)
<ハイドロゲルの製造>
水溶性のリチウム変性イソブテン-無水マレイン酸共重合樹脂(平均分子量325,000、中和度0.5、開環率96%)を用い、10重量%水溶液を調整して以下の試験で用いた。 <Test Example 2>
(Example 6)
<Manufacture of hydrogel>
A water-soluble lithium-modified isobutene-maleic anhydride copolymer resin (average molecular weight 325,000, neutralization degree 0.5, ring-opening rate 96%) was used, and a 10% by weight aqueous solution was prepared and used in the following tests. .
得られたハイドロゲルの透過率測定は10mmセルを用いて紫外・可視分光光度計(UV-2600シリーズ、島津製作所)にて測定した。可視光領域400nmから800nmの間での最も低い透過率の値を結果として表2に示す。 <Measurement of transmittance>
The transmittance of the obtained hydrogel was measured with an ultraviolet / visible spectrophotometer (UV-2600 series, Shimadzu Corporation) using a 10 mm cell. Table 2 shows the results of the lowest transmittance values in the visible light region between 400 nm and 800 nm.
Brookfield型粘度計(DV-I PRIMEブルックフィールド社製)を用いて25℃で、ポリエチレンイミン添加後(加熱前)のハイドロゲルの10重量%水溶液の粘度の測定を行った。ずり速度40s-1の時の粘度結果を下記表2に示す。 <Measurement of viscosity of hydrogel>
Using a Brookfield viscometer (DV-I PRIME Brookfield), the viscosity of a 10% by weight aqueous solution of hydrogel after addition of polyethyleneimine (before heating) was measured at 25 ° C. The viscosity results at a shear rate of 40 s -1 are shown in Table 2 below.
上記で作製した10重量%のハイドロゲルに当量の水を加え、ハンドミキサー(WARING STAND MIXER,WARING社製)を用いて、5重量%の負極用バインダー液を得た。 <Dilution of hydrogel>
An equivalent amount of water was added to 10% by weight of the hydrogel prepared above, and 5% by weight of a negative electrode binder liquid was obtained using a hand mixer (WARING STAND MIXER, manufactured by WARING).
負極用バインダー組成物の5重量%水溶液の代わりに、ハイドロゲルの5重量%水溶液を用いた以外は試験例1(実施例1)と同様にして、電極塗工用スラリーを作製した。スラリー中の活物質とハイドロゲルの組成比は固形分として、黒鉛粉末:導電助剤:ハイドロゲル(水分を除いたバインダー組成物としての重量)=100:1.075:6.452である。 <Preparation of slurry for negative electrode>
A slurry for electrode coating was prepared in the same manner as in Test Example 1 (Example 1) except that a 5 wt% aqueous solution of hydrogel was used instead of the 5 wt% aqueous solution of the negative electrode binder composition. The composition ratio of the active material and the hydrogel in the slurry is, as a solid content, graphite powder: conductive auxiliary agent: hydrogel (weight as a binder composition excluding moisture) = 100: 1.075: 6.452.
試験例1(実施例1)と同様にして、コイン電池用電極(電池用負極)を作製した。 <Preparation of negative electrode for battery>
A coin battery electrode (battery negative electrode) was prepared in the same manner as in Test Example 1 (Example 1).
試験例1(実施例1)の<剥離強度、靭性試験用電極の作製>と同様にして作製した電極を用いて試験を行った。 <Production of electrode for flexibility (toughness) test>
A test was performed using an electrode produced in the same manner as in <Preparation of peel strength and toughness test electrode> in Test Example 1 (Example 1).
電極の柔軟性(靭性)の評価は、試験例1(実施例1)の電極の靭性試験と同様にして行った。結果を下記表2に示す。 <Electrode flexibility (toughness) test>
The flexibility (toughness) of the electrode was evaluated in the same manner as the electrode toughness test of Test Example 1 (Example 1). The results are shown in Table 2 below.
試験例1(実施例1)の電極の靭性試験と同様にして、コイン電池(2032タイプ)を作製した。 <Production of battery>
A coin battery (2032 type) was produced in the same manner as the electrode toughness test of Test Example 1 (Example 1).
作製したコイン電池で、試験例1と同様の充放電試験を実施した。結果を下記表2に示す。 <Evaluation method: charge / discharge characteristic test>
With the produced coin battery, the same charge / discharge test as in Test Example 1 was performed. The results are shown in Table 2 below.
実施例6で用いた樹脂と架橋剤(PEI)を用いて、樹脂10重量%水溶液:PEI10重量%水溶液=99:1となるように、実施例6と同様の方法によってハイドロゲルを作製し、透過率及び粘度を測定した。結果を下記表2に示す。その後、実施例6と同様の方法によってハイドロゲルの希釈及び非水電解質電池用スラリー(負極用スラリー)を作製した。さらに、上記実施例6と同様の方法によって塗工負極(電池用負極)を作製し、コイン電池を得て、充放電特性試験を行った。また塗工電極(剥離強度、靱性試験用電極)を用いて、柔軟性試験を行った。結果を下記表2に示す。 (Example 7)
Using the resin and the crosslinking agent (PEI) used in Example 6, a hydrogel was prepared by the same method as in Example 6 so that the resin 10 wt% aqueous solution: PEI 10 wt% aqueous solution = 99: 1, Transmittance and viscosity were measured. The results are shown in Table 2 below. Then, the hydrogel dilution and the slurry for nonaqueous electrolyte batteries (slurry for negative electrodes) were produced by the same method as Example 6. Further, a coated negative electrode (battery negative electrode) was prepared by the same method as in Example 6 to obtain a coin battery, and a charge / discharge characteristic test was performed. In addition, a flexibility test was performed using a coated electrode (peel strength, toughness test electrode). The results are shown in Table 2 below.
水溶性のリチウム変性イソブテン-無水マレイン酸共重合樹脂(平均分子量325,000、中和度0.7、開環率97%)の10重量%水溶液を調製した。 (Example 8)
A 10% by weight aqueous solution of a water-soluble lithium-modified isobutene-maleic anhydride copolymer resin (average molecular weight 325,000, neutralization degree 0.7, ring opening rate 97%) was prepared.
水溶性のリチウム変性イソブテン-無水マレイン酸共重合樹脂(平均分子量325,000、中和度0.4、開環率92%)の10重量%水溶液を調製した。 Example 9
A 10% by weight aqueous solution of a water-soluble lithium-modified isobutene-maleic anhydride copolymer resin (average molecular weight 325,000, neutralization degree 0.4, ring opening rate 92%) was prepared.
実施例8で用いた樹脂と架橋剤(ポリアリルアミン、分子量3,000)を用いて、樹脂10重量%水溶液:PEI10重量%水溶液=99.34:0.66となるように、実施例6と同様の方法によってハイドロゲルを作製し、透過率及び粘度を測定した。結果を下記表2に示す。その後、実施例6と同様の方法によってハイドロゲルの希釈及び非水電解質電池用スラリーを作製した。さらに、上記実施例6と同様の方法によって塗工負極を作製し、コイン電池を得て、充放電特性試験を行った。また塗工電極を用いて、柔軟性試験及を行った。結果を下記表2に示す。 (Example 10)
Using the resin and the cross-linking agent (polyallylamine, molecular weight 3,000) used in Example 8, the resin 10% by weight aqueous solution: PEI 10% by weight aqueous solution = 99.34: 0.66 A hydrogel was prepared by the same method, and the transmittance and viscosity were measured. The results are shown in Table 2 below. Thereafter, a hydrogel dilution and a nonaqueous electrolyte battery slurry were prepared in the same manner as in Example 6. Further, a coated negative electrode was prepared by the same method as in Example 6 to obtain a coin battery, and a charge / discharge characteristic test was performed. Moreover, the flexibility test was done using the coating electrode. The results are shown in Table 2 below.
負極用バインダー組成物として水溶性のリチウム変性メチルビニルエーテル-無水マレイン酸共重合樹脂(平均分子量630,000、中和度0.5、開環率96%)の10重量%水溶液を調整した。 (Example 11)
As a negative electrode binder composition, a 10% by weight aqueous solution of a water-soluble lithium-modified methyl vinyl ether-maleic anhydride copolymer resin (average molecular weight 630,000, neutralization degree 0.5, ring opening rate 96%) was prepared.
水溶性のリチウム変性エチレン-無水マレイン酸共重合樹脂(平均分子量350,000、中和度0.5、開環率96%)の10重量%水溶液を調整した。 (Example 12)
A 10% by weight aqueous solution of a water-soluble lithium-modified ethylene-maleic anhydride copolymer resin (average molecular weight 350,000, neutralization degree 0.5, ring opening rate 96%) was prepared.
実施例6で用いた樹脂と架橋剤(PEI)を用いて、樹脂10重量%水溶液:PEI10重量%水溶液=90:10となるように、実施例6と同様の方法によってハイドロゲルを作製し、透過率及び粘度を測定した。結果を下記表2に示す。その後、実施例6と同様の方法によってハイドロゲルの希釈及び非水電解質電池用スラリーを作製した。さらに、上記実施例6と同様の方法によって塗工負極を作製し、コイン電池を得て、充放電特性試験を行った。また塗工電極を用いて、柔軟性試験を行った。結果を下記表2に示す。 (Comparative Example 5)
Using the resin and the crosslinking agent (PEI) used in Example 6, a hydrogel was prepared by the same method as in Example 6 so that the resin was 10 wt% aqueous solution: PEI 10 wt% aqueous solution = 90: 10, Transmittance and viscosity were measured. The results are shown in Table 2 below. Thereafter, a hydrogel dilution and a nonaqueous electrolyte battery slurry were prepared in the same manner as in Example 6. Further, a coated negative electrode was prepared by the same method as in Example 6 to obtain a coin battery, and a charge / discharge characteristic test was performed. Moreover, the flexibility test was done using the coated electrode. The results are shown in Table 2 below.
実施例7で用いた樹脂と架橋剤(PEI、分子量600)を用いて、実施例7と同様の方法によってハイドロゲルを作製し、透過率及び粘度を測定した。結果を下記表2に示す。その後、実施例6と同様の方法によってハイドロゲルの希釈及び非水電解質電池用スラリーを作製した。さらに、上記実施例6と同様の方法によって塗工負極を作製し、コイン電池を得て、充放電特性試験を行った。また塗工電極を用いて、柔軟性試験を行った。結果を下記表2に示す。 (Comparative Example 6)
Using the resin and crosslinking agent (PEI, molecular weight 600) used in Example 7, a hydrogel was prepared by the same method as in Example 7, and the transmittance and viscosity were measured. The results are shown in Table 2 below. Thereafter, a hydrogel dilution and a nonaqueous electrolyte battery slurry were prepared in the same manner as in Example 6. Further, a coated negative electrode was prepared by the same method as in Example 6 to obtain a coin battery, and a charge / discharge characteristic test was performed. Moreover, the flexibility test was done using the coated electrode. The results are shown in Table 2 below.
実施例6で用いた樹脂の10重量%水溶液(添加剤なし)の透過率及び粘度を測定した結果を下記表2に示す。その後、上記10重量%水溶液をバインダー溶液として用い、上記実施例6と同様の方法によって非水電解質電池用スラリーを作製した。さらに、上記実施例6と同様の方法によって塗工負極を作製し、コイン電池を得て、充放電特性試験を行った。また塗工電極を用いて、柔軟性試験を行った。結果を下記表2に示す。 (Comparative Example 7)
The results of measuring the transmittance and viscosity of a 10% by weight aqueous resin solution (no additive) used in Example 6 are shown in Table 2 below. Thereafter, a slurry for a non-aqueous electrolyte battery was produced in the same manner as in Example 6 using the 10 wt% aqueous solution as a binder solution. Further, a coated negative electrode was prepared by the same method as in Example 6 to obtain a coin battery, and a charge / discharge characteristic test was performed. Moreover, the flexibility test was done using the coated electrode. The results are shown in Table 2 below.
実施例10で用いた樹脂の10重量%水溶液(添加剤なし)の透過率及び粘度を測定した結果を下記表2に示す。その後、上記比較例7と同様の方法によって非水電解質電池用スラリーを作製した。次いで、上記実施例6と同様の方法によって塗工負極を作製し、コイン電池を得て、充放電特性試験を行った。また塗工電極を用いて、柔軟性試験を行った。結果を下記表2に示す。 (Comparative Example 8)
Table 2 below shows the results of measuring the transmittance and viscosity of a 10% by weight aqueous solution (without additives) of the resin used in Example 10. Then, the slurry for nonaqueous electrolyte batteries was produced by the method similar to the said comparative example 7. Subsequently, the coating negative electrode was produced by the method similar to the said Example 6, the coin battery was obtained, and the charge / discharge characteristic test was done. Moreover, the flexibility test was done using the coated electrode. The results are shown in Table 2 below.
実施例11で用いた樹脂の10重量%水溶液(添加剤なし)の粘度及び透過率を測定した結果を下記表2に示す。その後、上記比較例7と同様の方法によって非水電解質電池用スラリーを作製した。さらに、上記実施例6と同様の方法によって塗工負極を作製し、コイン電池を得て、充放電特性試験を行った。また塗工電極を用いて、柔軟性試験を行った。結果を下記表2に示す。 (Comparative Example 9)
The results of measuring the viscosity and transmittance of a 10% by weight aqueous solution of the resin used in Example 11 (without additives) are shown in Table 2 below. Then, the slurry for nonaqueous electrolyte batteries was produced by the method similar to the said comparative example 7. Further, a coated negative electrode was prepared by the same method as in Example 6 to obtain a coin battery, and a charge / discharge characteristic test was performed. Moreover, the flexibility test was done using the coated electrode. The results are shown in Table 2 below.
従来の水系負極バインダー組成物であるSBR系エマルジョン水溶液(TRD2001、48.3重量%)と増粘剤としてCMC-Na(セロゲンBSH-6、10重量%)を用いて上記比較例7と同様の方法によって非水電解質電池用スラリーを作製した。スラリー中の活物質とバインダーの組成比は固形分として、黒鉛粉末:導電助剤:SBR:CMC-Na=100:1.053:3.158:1.053であった。さらに、上記実施例6と同様の方法によって塗工負極を作製し、コイン電池を得て、充放電特性試験を行った。また塗工電極を用いて、柔軟性試験を行った。結果を下記表2に示す。 (Comparative Example 10)
Similar to Comparative Example 7 above, using an aqueous SBR emulsion aqueous solution (TRD2001, 48.3% by weight), which is a conventional aqueous negative electrode binder composition, and CMC-Na (cellogen BSH-6, 10% by weight) as a thickener. A slurry for a nonaqueous electrolyte battery was prepared by the method. The composition ratio between the active material and the binder in the slurry was, as a solid content, graphite powder: conductive aid: SBR: CMC-Na = 100: 1.053: 3.158: 1.053. Further, a coated negative electrode was prepared by the same method as in Example 6 to obtain a coin battery, and a charge / discharge characteristic test was performed. Moreover, the flexibility test was done using the coated electrode. The results are shown in Table 2 below.
本発明の所定の透過率を有するハイドロゲルを使用することによって、より柔軟性(靭性)が高い電極を作製できることが示された。また、本発明によれば、ハイドロゲル化するための架橋剤を添加しても、比較例7~9に示す未添加品と同等の低抵抗性を示し、比較例10に示した従来のバインダーであるSBR-CMC系よりも低く、電池特性向上に寄与することが分かった。これに対し、透過率が高い比較例6~9のハイドロゲルでは、十分に柔軟性を付与することができなかった。また、架橋剤の添加量が高く、透過率が低かった比較例5ではあまりにも粘度が高く、スラリー作製時の解砕が十分にできなかったため抵抗の高い電池となった。さらにポリアミン類の分子量が低い比較例6では架橋度が十分でなかったために粘度が低く、十分に柔軟性を付与することができなかった。 (Discussion)
It was shown that an electrode with higher flexibility (toughness) can be produced by using a hydrogel having a predetermined transmittance according to the present invention. Further, according to the present invention, even when a crosslinking agent for hydrogelation is added, the conventional binder shown in Comparative Example 10 shows low resistance equivalent to that of the non-added products shown in Comparative Examples 7 to 9. It was found to be lower than the SBR-CMC system, which contributes to improving battery characteristics. On the other hand, the hydrogels of Comparative Examples 6 to 9 having a high transmittance could not provide sufficient flexibility. Further, in Comparative Example 5 in which the addition amount of the cross-linking agent was high and the transmittance was low, the viscosity was too high, and crushing at the time of slurry preparation could not be sufficiently performed, resulting in a battery having high resistance. Furthermore, in Comparative Example 6 in which the molecular weight of the polyamines was low, the degree of crosslinking was not sufficient, so the viscosity was low, and sufficient flexibility could not be provided.
Claims (7)
- α-オレフィン類とマレイン酸類とが共重合したα-オレフィン-マレイン酸類共重合体の中和塩をポリアミン類で架橋した構造を含有する非水電解質電池電極用バインダー組成物であって、前記バインダー組成物を10重量%含有する水溶液の25℃且つずり速度40s-1における粘度が1800mPa・s~15000mPa・sであることを特徴とする、バインダー組成物。 A binder composition for a non-aqueous electrolyte battery electrode, comprising a structure in which a neutralized salt of an α-olefin-maleic acid copolymer obtained by copolymerizing an α-olefin and a maleic acid is crosslinked with a polyamine. A binder composition characterized in that an aqueous solution containing 10% by weight of the composition has a viscosity of 1800 mPa · s to 15000 mPa · s at 25 ° C. and a shear rate of 40 s −1 .
- 請求項1に記載のバインダー組成物から得られる、10重量%水溶液の可視光領域(400~800nm)における透過率が40~85%の範囲であるハイドロゲル。 A hydrogel obtained from the binder composition according to claim 1, having a transmittance of 40 to 85% in a visible light region (400 to 800 nm) of a 10% by weight aqueous solution.
- 請求項1に記載のバインダー組成物と活物質とを含有する、非水電解質電池電極用スラリー組成物。 A slurry composition for a nonaqueous electrolyte battery electrode, comprising the binder composition according to claim 1 and an active material.
- 請求項2に記載のハイドロゲルと活物質とを含有する、非水電解質電池電極用スラリー組成物。 A slurry composition for a nonaqueous electrolyte battery electrode, comprising the hydrogel according to claim 2 and an active material.
- 請求項1に記載のバインダー組成物と活物質とを含有する混合層を集電体に結着してなる、非水電解質電池用負極。 A negative electrode for a non-aqueous electrolyte battery, wherein a mixed layer containing the binder composition according to claim 1 and an active material is bound to a current collector.
- 請求項2に記載のハイドロゲルと活物質とを含有する混合層を集電体に結着してなる、非水電解質電池用負極。 A negative electrode for a non-aqueous electrolyte battery, wherein the mixed layer containing the hydrogel according to claim 2 and an active material is bound to a current collector.
- 請求項5または6に記載の非水電解質電池用負極を有する、非水電解質電池。
A nonaqueous electrolyte battery comprising the negative electrode for a nonaqueous electrolyte battery according to claim 5.
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CN201780073651.5A CN110024191A (en) | 2016-11-29 | 2017-11-21 | Nonaqueous electrolyte battery binder composition for electrode and its nonaqueous electrolyte battery slurry composition for electrode, nonaqueous electrolyte battery cathode and nonaqueous electrolyte battery as the hydrogel of raw material and is used using it |
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