JP5602465B2 - Battery electrode binder and battery electrode - Google Patents

Description

  The present invention relates to a battery electrode binder and a battery electrode prepared using the battery electrode binder.

  Lithium ion secondary batteries using an electrode active material that occludes and releases lithium ions as an electrode are gaining importance as a power source for small electronic devices because of their light weight and high energy density. In an electrode mainly composed of an electrode active material that absorbs and releases lithium ions, a polymer binder is usually used as a binder. The polymer binder is required to have adhesiveness with an active material, resistance to a polar solvent used as an electrolytic solution, and stability in an electrochemical environment. Conventionally, fluorine-based polymers such as polyvinylidene fluoride have been used in this field. However, when the electrode film is formed, the conductivity is hindered, and the adhesive strength between the current collector and the electrode film is insufficient. There is a problem. In addition, when a fluorine-based polymer is used for the negative electrode, which is a reducing condition, there are problems such as insufficient stability and a decrease in cycle performance of the secondary battery, and improvement of these problems is desired. . For this reason, development of non-fluorine polymers has been carried out. For example, Japanese Patent Laid-Open No. 63-121257 (Patent Document 1) describes an acrylonitrile-based polymer, and Japanese Patent Laid-Open No. 1-186557 (Patent Document 2) describes a polyester-based polymer. It is not enough to solve this problem.

JP 63-1212257 A

Japanese Patent Laid-Open No. 1-186557

  The objective of this invention is providing the battery electrode using the binder for battery electrodes with the favorable binding force at the time of making an electrode active material adhere to a collector, and the said binder for battery electrodes.

As a result of intensive studies to solve such problems, 4-phenylcyclohexene, which is a reaction product of 1,3-butadiene and styrene, which is by-produced in the polymerization process, is obtained as a copolymer latex used as a binder for battery electrodes. By limiting the amount to below a specific amount, the inventors have found that the above problems can be solved, and have completed the present invention.
That is, the present invention is a battery electrode binder, wherein the battery electrode binder is 1,3-butadiene 20-60 wt%, styrene 20-79 wt%, ethylenically unsaturated carboxylic acid monomer 0.1 A copolymer latex obtained by emulsion polymerization of a monomer composed of 10% by weight to 10% by weight, and another monomer copolymerizable with 0% to 59.9% by weight, and the copolymer A battery electrode binder and a battery electrode using the battery electrode binder, characterized in that 4-phenylcyclohexene remaining in the latex is 80 ppm or less based on the solid content of the copolymer latex It is.

  When the battery electrode binder of the present invention is used, a battery electrode having a good binding force between the current collector and the battery electrode composition, which is a mixture of the electrode active material and the battery electrode binder, is obtained.

The present invention is described in detail below.
Examples of the ethylenically unsaturated carboxylic acid monomer constituting the copolymer latex in the present invention include mono- or dicarboxylic acids (anhydrides) such as acrylic acid, methacrylic acid, crotonic acid, maleic acid, fumaric acid, and itaconic acid. Etc., and one or more of these can be used.

  Examples of other copolymerizable monomers constituting the copolymer latex in the present invention include alkenyl aromatic monomers (excluding styrene), unsaturated carboxylic acid alkyl ester monomers, and hydroxyalkyl groups. Examples thereof include unsaturated monomers, vinyl cyanide monomers, and unsaturated carboxylic acid amide monomers.

  Examples of the alkenyl aromatic monomer (excluding styrene) include α-methylstyrene, methyl α-methylstyrene, vinyltoluene and divinylbenzene, and these can be used alone or in combination of two or more.

  Unsaturated carboxylic acid alkyl ester monomers include methyl acrylate, methyl methacrylate, ethyl acrylate, ethyl methacrylate, butyl acrylate, glycidyl methacrylate, dimethyl fumarate, diethyl fumarate, dimethyl maleate, diethyl maleate, dimethyl itaconate , Monomethyl fumarate, monoethyl fumarate, 2-ethylhexyl acrylate, and the like, and one or more of them can be used. In particular, the use of methyl methacrylate is preferred.

  As unsaturated monomers containing a hydroxyalkyl group, β-hydroxyethyl acrylate, β-hydroxyethyl methacrylate, hydroxypropyl acrylate, hydroxypropyl methacrylate, hydroxybutyl acrylate, hydroxybutyl methacrylate, 3-chloro-2-hydroxypropyl methacrylate , Di- (ethylene glycol) maleate, di- (ethylene glycol) itaconate, 2-hydroxyethyl maleate, bis (2-hydroxyethyl) maleate, 2-hydroxyethyl methyl fumarate, and the like. Two or more types can be used. In particular, the use of β-hydroxyethyl acrylate is preferred.

  Examples of the vinyl cyanide monomer include acrylonitrile, methacrylonitrile, α-chloroacrylonitrile, α-ethylacrylonitrile, and the like, and one or more of them can be used. In particular, the use of acrylonitrile or methacrylonitrile is preferred.

  Examples of unsaturated carboxylic acid amide monomers include acrylamide, methacrylamide, N-methylol acrylamide, N-methylol methacrylamide, N, N-dimethylacrylamide, and the like, and one or more of these should be used. Can do. Particularly preferred is the use of acrylamide or methacrylamide.

  The monomer composition is 1,3-butadiene 20 to 60% by weight, styrene 20 to 79% by weight, ethylenically unsaturated carboxylic acid monomer 0.1 to 10% by weight, and copolymerizable therewith. It is composed of 0 to 59.9% by weight of other monomers.

  When 1,3-butadiene is less than 20% by weight, a sufficient binding force cannot be obtained when the battery electrode composition containing the binder for battery electrodes of the present invention is applied to the current collector, and 60% by weight is not obtained. When exceeding, the problem that electrolyte solution resistance falls when manufacturing the battery electrode of this invention is seen. Preferably it is 30 to 55% by weight.

  If the ethylenically unsaturated carboxylic acid monomer is less than 0.1% by weight, the stability of the copolymer latex itself and the battery electrode composition is poor, and if it exceeds 10% by weight, the viscosity of the latex increases. This creates a handling problem for the copolymer latex itself. Preferably it is 1 to 7 weight%.

  When the styrene is less than 20% by weight, the electrolytic solution resistance decreases when the battery is produced using the battery electrode of the present invention. When the styrene exceeds 79% by weight, the battery electrode composition containing the binder for the battery electrode of the present invention is obtained. When applied to the current collector, sufficient binding force with the electrode active material cannot be obtained. Preferably it is 38-69 weight%.

The amount of 4-phenylcyclohexene remaining in the copolymer latex of the present invention needs to be 80 ppm or less based on the solid content of the latex. When the residual amount of 4-phenylcyclohexene exceeds 80 ppm, a sufficient binding force cannot be obtained when the binder for battery electrodes of the present invention is mixed with an electrode active material and applied to a current collector. Preferably it is 40 ppm or less, More preferably, it is 20 ppm or less.
The method for reducing the amount of residual 4-phenylcyclohexene can be appropriately adjusted depending on the monomer composition of the copolymer latex, the addition method thereof, and the polymerization temperature. Furthermore, it can be appropriately adjusted depending on the conditions of steam distillation after polymerization and the conditions of reduced pressure treatment under heating. Of these conditions, the amount of residual 4-phenylcyclohexene can be reduced by setting the steam distillation temperature to 75 ° C or higher, more preferably 85 ° C or higher, and more preferably 98 ° C or higher. . As for the time for performing the steam distillation, for example, when compared at the same steam distillation temperature, when the time required to remove the unreacted monomer is used as a reference, the residual time is increased by at least 30%. The amount of 4-phenylcyclohexene can be reduced.

As the polymerization method of the copolymer latex of the present invention, any one of one-stage polymerization, two-stage polymerization, multi-stage polymerization, seed polymerization, power feed polymerization method and the like may be adopted. Further, the addition method of various components in the polymerization method of the present invention is not particularly limited, and any of a batch addition method, a divided addition method, and a continuous addition method can be employed.
Furthermore, when carrying out emulsion polymerization, usual emulsifiers, polymerization initiators, reducing agents, chain transfer agents, redox catalysts, hydrocarbon compounds, electrolytes, polymerization accelerators, chelating agents, and the like can be used.

  The emulsion polymerization of the present invention is carried out using water as a medium in the presence of an emulsifier. As the emulsifier used in the emulsion polymerization of the present invention, one or more of anionic surfactants, nonionic surfactants, amphoteric surfactants, and cationic surfactants are used alone or in combination. can do. Anionic surfactants include higher alcohol sulfates (sodium lauryl sulfate, sodium dodecyl sulfate), alkyl benzene sulfonates (sodium dodecyl benzene sulfonate, potassium dodecyl benzene sulfonate, ammonium dodecyl benzene sulfonate), alkyls Diphenyl ether sulfonate (sodium dodecyl diphenyl ether sulfonate, sodium dodecyl diphenyl ether disulfonate, disodium palmityl diphenyl oxide disulfonate), aliphatic sulfonate (α-olefin (C11-C15) sodium sulfonate, sodium lauryl sulfonate) , Ethoxylated sulfate (sodium alkylphenol ethoxylate sulfate), sulfosuccinic acid ester (dihexyls Sodium succinate, sodium dicyclohexylsulfosuccinate, sodium diamylsulfosuccinate, sodium diisobutylsulfosuccinate, disodium sulfosuccinate ethoxylated nonylphenol 1/2 ester tetrasodium N, (1,2-dicarboxyethyl) -N-octadecyl Sulfosuccinate, disodium isodecyl sulfosuccinate, sodium bistridecyl sulfosuccinate), sodium salt of condensed naphthalene sulfonate, alkyl allyl sulfonate (sodium salt of alkyl allyl sulfate), aliphatic carboxylate ( Lauric acid, stearic acid, montanic acid, behenic acid, sodium salt or potassium salt of palmitic acid), sulfate ester salt of nonionic surfactant (polyoxyethylene lauryl) Sodium ether sulfate, polyoxyethylene cetyl ether sodium sulfate, polyoxyethylene stearyl ether sodium sulfate, polyoxyalkylene alkyl ether sulfate salts such as sodium polyoxyethylene oleyl ether sulfate; polyoxyethylene nonylphenyl ether sodium sulfate, polyoxyethylene Polyoxyalkylene aryl ether sulfates such as sodium octylphenyl ether sulfate, polyoxyethylene (7) [distyrenated (methylphenyl ether)] ammonium sulfate ester, polyoxypropylene (8) [distyrenated (methylphenyl ether) ] Ammonium sulfate ester, polyoxyethylene (30) [distyrenated (methylphenyl ether)] sulfate Ammonium salt, polyoxyethylene (12) [distyrenated (butylphenyl ether)] sulfate sodium salt, polyoxyethylene (10) [methyldistyrenated (methylphenyl ether)] sulfate sodium salt, polyoxypropylene (20 ) [Methyl distyrenated (methyl phenyl ether)] sulfate sodium salt, [polyoxypropylene (5) polyoxyethylene (6)] random [distyrenated (methyl phenyl ether)] sulfate ammonium salt, [polyoxypropylene (10) Polyoxyethylene (20)] block [distyrenated methylphenyl ether)] sulfate sodium salt) and the like. Nonionic surfactants include polyethylene glycol alkyl ester type, alkyl phenyl ether type, alkyl ether type (polyethylene glycol monostearate, polyoxyethylene sorbitan lauryl ester, polyoxyethylene nonylphenyl ether, polyoxyethylene octyl). Phenyl ether, polyoxyethylene lauryl ether, polyoxyethylene stearyl ether) and the like. Further, as amphoteric surfactants, those of amino acid type such as salts of alkylbetaines such as lauryl betaine and stearyl betaine, lauryl-β-alanine, lauryl di (aminoethyl) glycine, octyldi (aminoethyl) glycine, etc. Etc.

  As the polymerization initiator, water-soluble polymerization initiators such as potassium persulfate, sodium persulfate, ammonium persulfate, cumene hydroperoxide, benzoyl peroxide, t-butyl hydroperoxide, acetyl peroxide, diisopropylbenzene hydroperoxide, An oil-soluble polymerization initiator such as 1,1,3,3-tetramethylbutyl hydroperoxide can be appropriately used. In particular, water-soluble polymerization initiators such as potassium persulfate, sodium persulfate and ammonium persulfate and oil-soluble polymerization initiators of cumene hydroperoxide are preferred.

  Specific examples of the reducing agent preferably used in the present invention include sulfite, bisulfite, pyrosulfite, nitrite, nithionate, thiosulfate, formaldehyde sulfonate, benzaldehyde sulfonate, Examples thereof include carboxylic acids such as L-ascorbic acid, erythorbic acid, tartaric acid and citric acid and salts thereof, reducing sugars such as dextrose and saccharose, and amines such as dimethylaniline and triethanolamine. In particular, L-ascorbic acid and erythorbic acid are preferable.

Examples of chain transfer agents that can be used in the present invention include α-methylstyrene dimer, n-hexyl mercaptan, n-octyl mercaptan, t-octyl mercaptan, n-dodecyl mercaptan, t-dodecyl mercaptan, n-stearyl mercaptan, and the like. Xanthogen compounds such as alkyl mercaptan, dimethylxanthogen disulfide, diisopropylxanthogen disulfide, thiuram compounds such as terpinolene, tetramethylthiuram disulfide, tetraethylthiuram disulfide, tetramethylthiuram monosulfide, 2,6-di-t-butyl- 4-methylphenol, phenolic compounds such as styrenated phenol, allyl compounds such as allyl alcohol, dichloromethane, dibromomethane, carbon tetrabromide Halogenated hydrocarbon compounds such as α-benzyloxystyrene, α-benzyloxyacrylonitrile, α-benzyloxyacrylamide, etc., vinyl ethers, triphenylethane, pentaphenylethane, acrolein, methacrolein, thioglycolic acid, thiomalic acid, 2 -Ethylhexyl thioglycolate etc. are mentioned, These can be used 1 type (s) or 2 or more types. In particular, n-octyl mercaptan and t-dodecyl mercaptan are preferable.
The amount of these chain transfer agents is not particularly limited, but is usually 0 to 5 parts by weight with respect to 100 parts by weight of the monomer.

  In the polymerization, saturated hydrocarbons such as pentane, hexane, heptane, octane, cyclohexane and cycloheptane, and unsaturated hydrocarbons such as pentene, hexene, heptene, cyclopentene, cyclohexene, cycloheptene, 4-methylcyclohexene and 1-methylcyclohexene. Hydrocarbon compounds such as aromatic hydrocarbons such as benzene, toluene and xylene may be used. In particular, cyclohexene having a moderately low boiling point and easily recovering and reusing components remaining as unreacted substances after the completion of polymerization by steam distillation or the like is suitable.

  Furthermore, anti-aging agents, preservatives, dispersants, thickeners and the like can be appropriately added to the copolymer latex as necessary.

  Although there is no restriction | limiting in particular about the gel content of the copolymer latex of this invention, From a viewpoint of the binding force of the composition for battery electrodes, and an electrode active material, preferable gel content is 40 to 100 weight%. When the gel content is less than 40%, the cohesive force as a polymer is small, and thus a sufficient binding force cannot be obtained.

  The number average particle size of the copolymer latex is not particularly limited, but a latex having a thickness of 50 to 250 nm is preferable. More preferably, it is 70-200 nm. If the number average particle diameter is less than 50 nm, the viscosity of the electrode composition is high and difficult to handle, and if it exceeds 250 nm, the change in the viscosity of the electrode composition with time increases.

  The binder for battery electrodes of this invention is used in order to form the electrode of secondary batteries, such as a lithium ion secondary battery, a nickel hydride battery, a nickel cadmium battery, for example. The particles of the positive electrode active material or the negative electrode constituent material and the positive electrode active material or the negative electrode constituent material and the current collector are bound together. Specifically, the composition for battery electrodes is prepared by blending the binder for battery electrodes of the present invention into the positive electrode active material or the negative electrode constituent material. That is, the composition for positive electrodes used for the positive electrode of a secondary battery is prepared by mix | blending the binder for battery electrodes with a positive electrode active material. Moreover, the composition for negative electrodes used for the negative electrode of a secondary battery is prepared by mix | blending the binder for battery electrodes with a negative electrode constituent material.

Below, the case where the binder for battery electrodes of this invention is used for a lithium ion secondary battery is demonstrated concretely.
The positive electrode active material is not particularly limited, but includes, for example, transition metal oxides such as MnO2, MoO3, V2O5, V6O13, Fe2O3, and Fe3O4, composite oxides including lithium such as LiCoO2, LiMnO2, LiNiO2, and LiXCoYSnZO2, LiFePO4, etc. Examples thereof include composite metal oxides containing lithium, for example, transition metal sulfides such as TiS2, TiS3, MoS3, and FeS2, for example, metal fluorides such as CuF2 and NiF2, and one kind or two or more kinds can be used.
The negative electrode constituent material is not particularly limited, but in the case of a non-aqueous electrolyte secondary battery, for example, carbon fluoride, graphite, carbon fiber, resin-fired carbon, linear graphite hybrid, coke, pyrolytic gas-layer-grown carbon Conductive carbonaceous materials such as calcined furfuryl alcohol resin, mesocarbon microbeads, mesophase pitch carbon, graphite whiskers, pseudo-isotropic carbon, fired natural materials, and pulverized products thereof, such as polyacene Examples thereof include conductive polymers such as organic semiconductors, polyacetylene, poly-p-phenylene, and the like, and one kind or two or more kinds can be used.
When preparing a battery electrode composition, the solid content of the copolymer latex is, for example, 0.1 to 10 parts by weight with respect to 100 parts by weight of the positive electrode active material or the negative electrode constituent material. Preferably, it mix | blends so that it may become 0.5-5 weight part. If the blending amount of the binder for battery electrodes of the present invention is less than 0.1 parts by weight, a good binding force to the current collector cannot be obtained, and if it exceeds 10 parts by weight, the electrical resistance increases and the battery characteristics are adversely affected.

  Various additives such as a water-soluble thickener may be added to the battery electrode binder of the present invention as necessary. Examples include water-soluble thickeners such as carboxymethyl cellulose, methyl cellulose, hydroxymethyl cellulose, ethyl cellulose, polyvinyl alcohol, polyacrylic acid (salt), oxidized starch, phosphorylated starch, casein, hexametaphosphate soda, tripolyphosphate soda, pyrophosphate soda , Dispersants such as sodium polyacrylate, and nonionic and anionic surfactants as latex stabilizers.

  The binder for battery electrodes of the present invention is used as a battery electrode by mixing with an electrode active material (positive electrode active material or negative electrode constituent material), applying it to a slurry and applying it to a current collector, followed by drying. In addition, as a method of applying the slurry to the current collector, any coater head such as a reverse roll method, a comma bar method, a gravure method, and an air knife method can be used. A wind dryer, an infrared heater, a far infrared heater, etc. can be used. The drying temperature is usually 50 ° C. or higher.

  When manufacturing a battery using the binder for battery electrodes of the present invention, existing ones such as a current collector, a separator, a non-aqueous electrolyte, a terminal, an insulator, and a battery container can be used without any particular limitation.

  EXAMPLES Hereinafter, although an Example is given and this invention is demonstrated more concretely, this invention is not limited to these Examples, unless the summary is changed. In the examples, parts and percentages indicating percentages are based on weight. Moreover, the preparation method of copolymer latex in an Example and evaluation of various physical properties were based on the following method.

Measurement of particle diameter of copolymer latex The number average particle diameter of the copolymer latex was measured by a dynamic light scattering method. In the measurement, FPAR-1000 (manufactured by Otsuka Electronics) was used.

Measurement of Residual 4-Phenylcyclohexene in Copolymer Latex Residual 4-phenylcyclohexene in the copolymer latex was measured by the following method using a gas chromatograph GC-14A manufactured by Shimadzu Corporation.
(1) Preparation of sample 1 g of copolymer latex (solid content: 45 to 50% by weight) was precisely weighed, dissolved in 25 ml of acetone and allowed to stand in a sealed container for 24 hours, and this was used as a measurement sample.
(2) Gas chromatograph measurement conditions Sample volume: 5 μl
Detector: FID
Inj / Det temperature: 200 ° C
Column temperature: After 80 ° C. × 40 min, 180 ° C. × 20 min
Column: Glass column 20m x 1.2mmφ
Stationary phase: Methyl silicon Liquid film thickness: 3μm
Carrier gas: helium, 20 ml / min.
Hydrogen: 0.7kg / cm2
Air: 0.9kg / cm2
(3) Quantitative Method Using a calibration curve prepared using a known concentration of phenylcyclohexane, the quantitative value of phenylcyclohexane relative to the copolymer latex solid content was determined as residual 4-phenylcyclohexene from the obtained gas chromatograph. The same sample was measured three times, and the average value was shown in units of ppm.

Measurement of gel content of copolymer latex A latex film is prepared at room temperature. Thereafter, about 1 g of the latex film is weighed and placed in 400 cc of toluene to swell and dissolve for 48 hours. Thereafter, this was filtered through a 300-mesh wire mesh, and the toluene-insoluble portion trapped in the wire mesh was dried and weighed. Calculated with

Preparation of copolymer latex (1), (2), (5), (7) In a pressure-resistant polymerization reactor, 120 parts of polymerization water, 0.6 part of sodium dodecylbenzenesulfonate as an emulsifier, 0 parts of sodium bicarbonate .2 parts, 0.9 part of potassium persulfate, and 8 parts of cyclohexene were added and stirred well. Then, each monomer in the first stage shown in Tables 1 and 2 and t-dodecyl mercaptan were added, and 1 at 60 ° C. was added. Time polymerization is performed, the temperature is raised to 70 ° C., and each monomer and t-dodecyl mercaptan shown in the second stage of Table 1 and Table 2 are continuously added in 7 hours, and then the polymerization conversion becomes 97%. Until the polymerization was continued.
Subsequently, these copolymer latexes were subjected to steam distillation under the conditions shown in Tables 1 and 2 to remove unreacted monomers and the like, and the particle diameters, gel contents, 4 -Copolymer latex (1), (2), (5), (7) having an amount of phenylcyclohexene was obtained.

Preparation of copolymer latex (3) In a pressure resistant polymerization reactor, 120 parts of polymerization water, 0.6 part of sodium dodecylbenzenesulfonate as an emulsifier, 0.2 part of sodium bicarbonate, 0.9 part of potassium persulfate, After charging 8 parts of cyclohexene and stirring sufficiently, each monomer in the first stage shown in Table 1 and t-dodecyl mercaptan were added, polymerization was performed at 60 ° C. for 1 hour, and the temperature was raised to 65 ° C. After continuously adding each monomer and t-dodecyl mercaptan shown in the second stage in 4 hours, the temperature was further raised to 70 ° C., and each monomer and t-dodecyl mercaptan shown in the third stage in Table 1 were added. Was added continuously over 3 hours. Further, the polymerization was continued until the polymerization conversion rate reached 97%.
Subsequently, these copolymer latexes are subjected to steam distillation under the conditions shown in Table 1 to remove unreacted monomers and the like, and the particle sizes, gel contents, and 4-phenylcyclohexene amounts shown in Table 1 are co-polymerized. A polymer latex (3) was obtained.

Preparation of copolymer latex (4) 120 parts of polymerization water in a pressure-resistant polymerization reactor, 0.6 parts of sodium dodecylbenzenesulfonate as an emulsifier, 0.2 part of sodium bicarbonate, 0.9 part of potassium persulfate, cyclohexene After 8 parts were charged and sufficiently stirred, each monomer in the first stage shown in Table 2 and t-dodecyl mercaptan were added and polymerization was carried out at 55 ° C for 1 hour, and the temperature was raised to 70 ° C. After continuously adding each monomer shown in the second stage and t-dodecyl mercaptan in 3 hours, the polymerization was continued until the polymerization conversion reached 97%.
Subsequently, these copolymer latexes are subjected to steam distillation under the conditions shown in Table 2 to remove unreacted monomers and the like, and the particle diameter, gel content, and 4-phenylcyclohexene content shown in Table 2 are co-polymerized. A polymer latex (4) was obtained.

Preparation of copolymer latex (6) In a pressure resistant polymerization reactor, 120 parts of polymerization water, 0.6 part of sodium dodecylbenzenesulfonate as an emulsifier, 0.2 part of sodium bicarbonate, 0.9 part of potassium persulfate, After charging 8 parts of cyclohexene and stirring sufficiently, each monomer in the first stage shown in Table 2 and t-dodecyl mercaptan were added, polymerization was conducted at 60 ° C. for 1 hour, and the temperature was raised to 70 ° C. After continuously adding each monomer and t-dodecyl mercaptan shown in the second stage in 7 hours, the polymerization was continued until the polymerization conversion reached 97%.
Subsequently, these copolymer latexes are subjected to steam distillation under the conditions shown in Table 2 to remove unreacted monomers and the like, and the particle diameter, gel content, and 4-phenylcyclohexene content shown in Table 2 are co-polymerized. A polymer latex (6) was obtained.

Preparation of electrode composition
(1) Preparation of positive electrode composition 100 parts by weight of LiCoO2 as a positive electrode active material, 5 parts by weight of acetylene black as a conductive agent, and 4 parts by weight of copolymer latex (1) to (7) as a binder An appropriate amount of water was added and kneaded so that the total solid content was 40%, to prepare a positive electrode composition slurry.
(2) Preparation of composition for negative electrode Natural graphite having an average particle diameter of 20 μm is used as a negative electrode constituent material, and 2 parts by weight of a carboxymethyl cellulose aqueous solution as a thickener is added to 100 parts by weight of natural graphite. An appropriate amount of water was added and kneaded with 4 parts by weight of the polymer latexes (1) to (7) so that the total solid content was 40%, thereby preparing a composition slurry for a negative electrode.

Preparation of electrode (1) Preparation of positive electrode Each positive electrode composition was applied to both sides of a 20 μm thick aluminum foil serving as a current collector, dried at 120 ° C. for 20 minutes, and compression-molded with a press (room temperature). Then, positive electrodes of Examples 1 to 3 and Comparative Examples 1 to 4 were prepared. A positive electrode having a coating layer thickness of 80 μm (per one side) was obtained. The contents of these evaluations are as follows.
(2) Preparation of Negative Electrode Each negative electrode composition was applied to both sides of a 20 μm thick copper foil serving as a current collector, dried at 120 ° C. for 20 minutes, and compression molded with a press (room temperature). 1 to 3 and Comparative Examples 1 to 4 were prepared. A negative electrode having a coating layer thickness of 80 μm (per one side) was obtained. The contents of these evaluations are as follows.

Evaluation of binding force of electrode coating layer On the surface of the electrode sheet obtained by the above-mentioned method, using a knife, 6 notches from the coating layer to the depth reaching the current collector are placed at 2 mm intervals vertically and horizontally, 25 A grid having (5 × 5) grids was formed. An adhesive tape was applied to the cut and immediately peeled off, and the degree of the active material falling off was visually evaluated as follows. The evaluation results are shown in Tables 1 and 2.
◎: No dropout ○: 1-9 squares dropped Δ: 10-19 squares dropped ×: 20-25 squares dropped

  Copolymer latex (4) and (5) are copolymer latex having the same composition ratio as copolymer latex (1), but the residual 4-phenylcyclohexene exceeded 80 ppm. In Examples 1 and 2, the binding force was inferior. The copolymer latex (6) had a residual 4-phenylcyclohexene of 80 ppm or less, but the composition ratio of 1,3-butadiene was 60% by weight or more. Was inferior. Furthermore, since the copolymer latex (7) does not use an ethylenically unsaturated carboxylic acid monomer and is outside the lower limit of the claims, the binding force was inferior in Comparative Example 4 using the copolymer latex (7).

  When the battery electrode binder of the present invention is used, a battery electrode having a good binding force between the current collector and the battery electrode composition, which is a mixture of the electrode active material and the battery electrode binder, is obtained.

Claims (3)

1,3-butadiene 20-60% by weight, styrene 20-79% by weight, ethylenically unsaturated carboxylic acid monomer 0.1-10% by weight, other monomers copolymerizable with these 0-59 A copolymer latex obtained by emulsion polymerization of a monomer composed of 9% by weight, wherein 4-phenylcyclohexene remaining in the copolymer latex is a solid content of the copolymer latex. The binder for battery electrodes characterized by being 80 ppm or less with respect to this.   The binder for battery electrodes, wherein 4-phenylcyclohexene remaining in the copolymer latex according to claim 1 is 20 ppm or less based on the solid content of the copolymer latex. The battery electrode using the binder for battery electrodes of Claim 1 or Claim 2.