JP2013120710A - Manufacturing method of electrode for secondary battery, manufacturing method of paint for secondary battery, electrode for secondary battery, and secondary battery - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a manufacturing method of the electrode for a secondary battery ensuring excellent peeling strength of an electrode mixture and a collector and capable of exhibiting the function as a battery sufficiently, by obtaining a paint for secondary battery having excellent coating properties and drying properties, and to provide a manufacturing method of a paint for secondary battery, an electrode for secondary battery and a secondary battery.SOLUTION: The manufacturing method of the electrode for a secondary battery includes a mixing step for preparing a slurry by mixing an active material, a binder, and a solvent, a stirring step for preparing a paint for secondary battery by stirring the slurry, and a coating step for coating a collector with the paint for secondary battery. In the stirring step, the slurry is stirred at a shear rate three times or more the maximum shear rate to which the paint for secondary battery is exposed in the coating step.

Description

 The present invention relates to a method for producing a secondary battery electrode, a method for producing a secondary battery paint, a secondary battery electrode, and a secondary battery.

The manufacturing process of the secondary battery electrode includes a mixing process, a stirring process, a coating process, a drying process, a pressing process, and a heat treatment process.
In the mixing step, the active material, the binder, and the solvent are mixed to prepare a slurry. When the active material is a positive electrode active material, a conductive material is further included.
In the stirring step, the slurry obtained in the mixing step is stirred to prepare a secondary battery paint.
In the preparation of the secondary battery paint, the mixing step and the stirring step may be performed simultaneously.
In the coating process, a secondary battery paint is applied to a current collector such as an aluminum foil or a copper foil.
In the drying step, the secondary battery paint applied to the current collector is dried to remove the solvent contained in the secondary battery paint, and the electrode mixture is fixed onto the current collector. An unpressed electrode is produced.
Further, in the pressing step, the unpressed electrode is pressed by a roll press or the like to produce a pressed electrode in which the density and the porosity of the electrode mixture fixed on the current collector are adjusted.
In the heat treatment step, the press electrode is heat-treated to completely remove the residual solvent in the electrode mixture, relax the residual stress of the electrode, and improve the adhesion of the electrode mixture to the current collector. Thus, an electrode for a secondary battery is obtained.

The secondary battery electrode is manufactured using the secondary battery electrode that the particle size distribution, film thickness distribution, and density distribution of the electrode mixture fixed to the current collector at any part of the electrode are uniform. It is important for exhibiting the function as a secondary battery. If there is variation in the composition distribution, film thickness distribution, and density distribution of the electrode mixture in the secondary battery electrode, the adhesion between the electrode mixture and the current collector will be partially reduced in the electrode in the secondary battery. As a result, the electrode structure may change or the current density may become uneven, which may cause the charge / discharge characteristics of the secondary battery to not be fully exhibited, or the rate characteristics, cycle characteristics, and life characteristics to deteriorate. .
In order to produce a secondary battery electrode with a uniform particle size distribution, film thickness distribution, and density distribution of the electrode mixture, a secondary battery paint having a uniform particle size distribution is prepared and applied by a mixing step and a stirring step. In the manufacturing process and the drying process, it is important to produce an unpressed electrode having a uniform film thickness distribution.

In particular, in the preparation of a coating material for a secondary battery, when a material having a small particle diameter and a large surface area is included as a constituent material of the coating material, the particles are highly cohesive. A large shear force is required in the space. Therefore, when a secondary battery electrode including an active material or conductive material having a small particle diameter and a large surface area is prepared, a secondary battery paint having sufficiently uniform particle dispersibility is prepared in the stirring step. There is a need.
When a secondary battery electrode is produced using a secondary battery paint with insufficient particle dispersibility, and the secondary battery is produced using the secondary battery electrode, the obtained secondary battery is a battery. The function as can not be fully demonstrated. Also, when a secondary battery paint with insufficient particle dispersibility is used, poor coating such as rubbing occurs in the coating process, electrode cracking occurs in the drying process, and drying is insufficient. Or the film thickness distribution of the obtained electrode is not uniform, or the adhesion between the electrode mixture and the current collector is insufficient.

As a technique for producing a coating material for a secondary battery including such a positive electrode material having a small particle diameter as an active material, a method of mixing and stirring slurry using a thin-film swirling stirrer is disclosed (for example, (See Patent Document 1 and Patent Document 2).
In Patent Document 1, a positive electrode mixture layer is obtained by using a thin-film swirl stirrer in a stirring step in the preparation of a secondary battery coating material including an olivine-based positive electrode active material having conductive glaze particles arranged on the surface. Can be prevented from peeling from the current collector, and a secondary battery electrode excellent in battery performance can be stably produced.
Patent Document 2 discloses that a thin-film swirl stirrer is used in the stirring step in the preparation of a secondary battery paint including a positive electrode powder composed of particles having a particle diameter of 0.05 μm or more and 1 μm or less. It is disclosed.

JP 2009-259698 A JP 2011-70994 A

 However, a new problem has been found that when the coating speed is increased in order to improve productivity, the obtained secondary battery electrode causes coating defects such as rubbing. Thus, there has been a demand for a method for producing an electrode for a secondary battery with good coating properties that does not cause poor coating even at a high coating speed.

 The present invention has been made in view of the above circumstances, and obtains a coating material for a secondary battery having good coating properties and good drying properties, and the peel strength between the electrode mixture and the current collector is good. Therefore, it is an object of the present invention to provide a method for manufacturing a secondary battery electrode, a method for manufacturing a secondary battery paint, a secondary battery electrode, and a secondary battery that can sufficiently exhibit a battery function.

 As a result of intensive studies to solve the above problems, the present inventors have found that the following inventions meet the above problems, and have completed the present invention.

That is, the present invention relates to the following inventions.
The method for producing an electrode for a secondary battery of the present invention includes a mixing step of preparing a slurry by mixing an active material, a binder, and a solvent, and an agitation step of adjusting the paint for a secondary battery by stirring the slurry. And a coating step of applying the secondary battery coating material to a current collector, wherein the secondary battery coating material is applied in the stirring step. The slurry is agitated at a shear rate of 3 times or more than the maximum shear rate exposed in step (1).

In the method for producing an electrode for a secondary battery of the present invention, it is preferable that the maximum shear rate exposed in the coating step is 1500 s ⁻¹ or more.

 In the method for producing an electrode for a secondary battery of the present invention, it is preferable that the slurry further contains a conductive material.

 In the method for producing an electrode for a secondary battery of the present invention, it is preferable that a particle diameter of the active material is 0.005 to 5 μm.

In the method for producing an electrode for a secondary battery of the present invention, the specific surface area of the active material is preferably 5 to 100 m ² / g.

 In the method for producing an electrode for a secondary battery of the present invention, it is preferable that the transition metal element constituting the active material is at least one selected from the group consisting of manganese, nickel, and cobalt.

 In the method for producing an electrode for a secondary battery of the present invention, it is preferable that the crystal structure of the active material is a layered structure.

 In the method for manufacturing an electrode for a secondary battery of the present invention, it is preferable that the conductive material contains carbon black.

 In the method for producing an electrode for a secondary battery of the present invention, it is preferable to use a stirring device that stirs by a rotating thin film method in the stirring step.

In the method for producing an electrode for a secondary battery of the present invention, it is preferable that a shear rate for stirring the slurry is 7500 s ⁻¹ or more.

 The method for producing a coating material for a secondary battery according to the present invention includes a mixing step in which a slurry is prepared by mixing an active material, a binder, and a solvent, and a stirring step in which the slurry is stirred to prepare a coating material for a secondary battery. And in the stirring step, the secondary battery paint has a shear rate of 3 times or more than the maximum shear rate to which the secondary battery paint is exposed in the coating step. The slurry is stirred.

 The secondary battery electrode of the present invention is manufactured by the method for manufacturing a secondary battery electrode of the present invention.

 The secondary battery of the present invention includes the secondary battery electrode of the present invention.

 According to the method for producing an electrode for a secondary battery of the present invention, an electrode for a secondary battery can be obtained which has a good peel strength between the electrode mixture and the current collector and can sufficiently exhibit the function as a battery. In particular, according to the method for producing a secondary battery electrode of the present invention, a secondary battery electrode can be obtained with high productivity without causing poor coating of the secondary battery paint even at a high coating speed.

Embodiments of a method for manufacturing a secondary battery electrode, a method for manufacturing a secondary battery paint, a secondary battery electrode, and a secondary battery according to the present invention will be described.
Note that this embodiment is specifically described in order to better understand the gist of the invention, and does not limit the present invention unless otherwise specified.

 The method for producing an electrode for a secondary battery of the present invention includes an agitation step of preparing a secondary battery coating material by stirring a slurry containing an active material, a binder, and a solvent. This is a method of stirring the slurry at a shear rate of 3 times or more than the maximum shear rate at which the coating material is exposed in the coating process. In the manufacturing method of the electrode for secondary batteries of this invention, it is preferable that a slurry contains a electrically conductive material further.

<Electrode for secondary battery>
The secondary battery electrode is an electrode used for producing a secondary battery.
The electrode for a secondary battery has a structure in which a layer made of an electrode mixture containing an active material is laminated on a current collector.
There are a positive electrode and a negative electrode as electrodes used in the secondary battery. In the positive electrode, the positive electrode active material is contained in the electrode mixture. In the negative electrode, the negative electrode active material is contained in the electrode mixture.
In general, the secondary battery electrode is obtained by applying the secondary battery paint obtained in the manufacturing process of the secondary battery paint to the current collector in the coating process, and further in the drying process. It is obtained by removing the solvent contained in the secondary battery coating material by drying the secondary battery coating material applied to the secondary battery.

[Current collector]
As the current collector, a conductor such as aluminum foil, nickel foil, stainless steel foil, or copper foil is used.
As the current collector for the positive electrode, an aluminum foil is preferable because it is stable at the positive electrode operating potential of the secondary battery, is easily processed into a thin film, and is inexpensive.
The negative electrode current collector is preferably a copper foil because it is stable at the negative electrode operating potential of the secondary battery and can be easily processed into a thin film.

[Secondary battery paint]
The secondary battery paint is a paint for producing a secondary battery electrode.
The secondary battery paint is composed of a solvent, a binder, an active material, a conductive material, and the like.
The secondary battery paint is produced through a secondary battery paint production process including a mixing step and a stirring step.
In addition, secondary battery paints can have flow characteristics and drying characteristics suitable for the capabilities of the equipment used in the coating process and drying process by adjusting the components and composition of the paint and adjusting the preparation conditions of the paint. To be made.

{solvent}
As the solvent, an aqueous solvent or an organic solvent is used.
Examples of the organic solvent include amine solvents such as N, N-dimethylaminopropylamine and diethylenetriamine; ether solvents such as tetrahydrofuran; ketone solvents such as methyl ethyl ketone; ester solvents such as methyl acetate; dimethylacetamide, N-methyl- Examples thereof include amide solvents such as 2-pyrrolidone (hereinafter sometimes referred to as “NMP”).
If necessary, a binder may be added to the solvent. Examples of the binder include carboxymethyl cellulose, sodium polyacrylate, polyvinyl alcohol, and polyvinyl pyrrolidone.

{Active material}
As the active material, a material capable of electrochemical charging and discharging is used.
Specifically, as the active material, lithium, oxygen, carbon, fluorine, sodium, magnesium, aluminum, silicon, phosphorus, sulfur, potassium, calcium, titanium, vanadium, chromium, manganese, iron, cobalt, nickel, copper, Examples include zinc, gallium, yttrium, niobium, molybdenum, silver, indium, and tungsten as constituent elements.

The particle diameter of the active material is usually 0.001 to 100 μm. The particle diameter of the active material is preferably 0.005 to 5 μm, more preferably 0.01 to 1 μm, and still more preferably 0.05 to 0.5 μm.
The particle diameter of the primary particles of the active material can be measured from a scanning electron microscope (SEM) photograph of the active material.

The specific surface area of the active material is usually 0.01 to ²⁰⁰ m ² / g, preferably 5 to 100 m ² / g.
The specific surface area of the active material can be measured by measuring the BET specific surface area using nitrogen gas.
For the measurement of the BET specific surface area, a specific surface area meter by a gas adsorption method or a specific surface area meter by a mercury intrusion method can be used.

(Positive electrode active material)
Examples of the positive electrode active material include chalcogen compounds (oxides, sulfides, and the like), and materials that can be electrochemically charged and discharged at a higher potential than the negative electrode. These positive electrode active materials are used alone or in combination of two or more.
Specific examples of the positive electrode active material include lithium, oxygen, sodium, magnesium, aluminum, tin, sulfur, vanadium, manganese, iron, nickel, copper, cobalt, gallium, molybdenum, indium, and tungsten as constituent elements. Is mentioned. Among these, particularly preferably, the transition metal element constituting the positive electrode active material is at least one selected from the group consisting of manganese, nickel and cobalt, and most preferably the alkali metal constituting the positive electrode active material The element is at least one selected from the group consisting of lithium and sodium.

Hereinafter, a positive electrode active material is illustrated.
Specific examples of the oxide include transition metal oxides, alkali metal transition metal composite oxides having a layered structure, alkali metal transition metal composite oxides having a spinel structure, and alkali metal transition metal composite oxides having an olivine structure. And an alkali metal transition metal complex oxide having a composition of Li ₂ MO ₃ (where M is a transition metal), and solid solutions thereof.
The transition metal oxide is an oxide represented by a composition of M _x O _y (where M is a transition metal and x and y are positive real numbers), specifically, MnO ₂ , _{V 2 O 5, Cr 3 O} 8 and the like.
Examples of the alkali metal transition metal complex oxide having a layered structure include a complex oxide represented by a composition of LiMO ₂ (where M is a transition metal), specifically, LiCoO _2. , LiNiO ₂ , LiNi _1/3 Co _1/3 Mn _1/3 O ₂ , LiNi _0.5 Co _0.2 Mn _0.3 O ₂ , and solid solutions thereof.

Examples of the alkali metal transition metal composite oxide having a spinel structure include a composite oxide represented by a composition of LiM ₂ O ₄ (where M is a transition metal). Examples include LiMn ₂ O ₄ and LiNi _1/2 Mn _3/2 O ₄ .
Examples of the alkali metal transition metal composite oxide having an olivine structure include a composite oxide represented by a composition of LiMPO ₄ (where M is a transition metal). Specifically, LiFePO ₄ , LiMnPO ₄ , LiCoPO ₄ , and solid solutions thereof.
Specific examples of the alkali metal transition metal composite oxide having a composition of Li ₂ MO ₃ (where M is a transition metal) include Li ₂ MnO ₃ .

In addition to the above oxide, an alkali metal transition metal composite oxide having a composition of Li ₂ MSiO ₄ (where M is a transition metal) such as Li ₂ FeSiO ₄ is used as the oxide. .

Specific examples of the sulfide include a sulfide having a composition of M _x O _y (where M is a transition metal, and x and y are positive real numbers).
Examples of the _{sulfide, Fe x S y, Ni x} S y, Mn x S y, Co x S y, include _Mo x _{S y.}

These oxides and sulfides may be used in combination, and may be crystalline or amorphous.
Further, these oxides and sulfides are mainly used as a positive electrode current collector and used as an electrode (positive electrode).

The crystal structure of the positive electrode active material is not particularly limited, but a preferable crystal structure includes a layered structure. The crystal structure of the positive electrode active material is more preferably a hexagonal or monoclinic crystal structure.
The hexagonal crystal structure is P3, P3 ₁ , P3 ₂ , R3, P-3, R-3, P312, P321, P3 ₁ 12, P3 ₁ 21, P3 ₂ 12, P3 ₂ 21, R32, P3m1. , P31m, P3c1, P31c, R3m, R3c, P-31m, P-31c, P-3m1, P-3c1, R-3m, R-3c, P6, P6 ₁ , P6 ₅ , P6 ₂ , P6 ₄ , P6 ₃ , P-6, P6 / m, P6 ₃ / m, P622, P6 ₁ 22, P6 ₅ 22, P6 ₂ 22, P6 ₄ 22, P6 ₃ 22, P6mm, P6cc, P6 ₃ cm, P6 ₃ mc, P It belongs to any one space group selected from the group consisting of -6m2, P-6c2, P-62m, P-62c, P6 / mmm, P6 / mcc, P6 ₃ / mcm and P6 ₃ / mmc.
The monoclinic crystal structures are P2, P2 ₁ , C2, Pm, Pc, Cm, Cc, P2 / m, P2 ₁ / m, C2 / m, P2 / c, P2 ₁ / c and C2 / c. Belonging to any one space group selected from the group consisting of
More preferably, it is preferable that the crystal structure of the positive electrode active material belongs to a space group of R-3m included in the hexagonal crystal structure or a C2 / m space group included in the monoclinic crystal structure.

 The crystal structure of the active material is identified from a powder X-ray diffraction pattern obtained by powder X-ray diffraction measurement using CuKα rays as a radiation source. As the X-ray source in the powder X-ray diffraction measurement, CoKα ray, MoKα ray or WKα ray is used in addition to CuKα ray.

(Negative electrode active material)
Examples of the negative electrode active material include carbon materials, chalcogen compounds (oxides, sulfides, and the like), nitrides, metals, and alloys, and materials that can be electrochemically charged and discharged at a lower potential than the positive electrode. . These negative electrode active materials are used alone or in combination of two or more.

Hereinafter, a negative electrode active material is illustrated.
Specific examples of the carbon material include graphites such as natural graphite and artificial graphite, cokes, carbon black, pyrolytic carbons, carbon fibers, and organic polymer compound fired bodies.
Specific examples of the oxide include silicon oxide represented by the formula SiO _x such as SiO ₂ and SiO (where x is a positive real number); the formula TiO _x such as TiO ₂ and TiO ( Here, x is a positive real number.) A titanium oxide represented by: Vadium represented by the formula VO _x (where x is a positive real number) such as V ₂ O ₅ and VO ₂ . An oxide of iron represented by the formula FeO _x (where x is a positive real number) such as Fe ₃ O ₄ , Fe ₂ O ₃ , FeO; SnO _x such as SnO ₂ and SnO ( Here, x is a positive real number.) A tin oxide represented by: WO ₃ , WO _{2 and} other general formulas WO _x (where x is a positive real number) _oxide; Li ₄ Ti ₅ O 12, Li and titanium, such as LiVO ₂ and / or It can be mentioned composite metal oxide containing vanadium.

Specifically, as the sulfide, titanium sulfide represented by the formula TiS _x (where x is a positive real number) such as Ti ₂ S ₃ , TiS ₂ , and TiS; V ₃ S ₄ , VS ₂ , VS, etc., and vanadium sulfide represented by the formula VS _x (where x is a positive real number); Fe ₃ S ₄ , FeS ₂ , FeS, and other formulas FeS _x where x is An iron sulfide represented by a positive real number; a molybdenum sulfide represented by the formula MoS _x (where x is a positive real number) such as Mo ₂ S ₃ and MoS ₂ ; SnS ₂ , SnS and the like SnS _x represented by the formula SnS _x (where x is a positive real number); WS _{2 and} other formulas WS _x (where x is a positive real number) sulfides of tungsten is; _Sb 2 _{S 3,} etc. formula SbS _x (wherein, x represents a positive real number der Antimony represented _{by);.. Se 5 S 3} , SeS 2, SeS formula SeS _x (wherein, etc., x is sulfide selenium represented by a positive real number) and the like.

Specific examples of the nitride include lithium-containing nitride such as Li ₃ N, Li _3-x A _x N (where A is Ni and / or Co, and O <x <3). Things.

These carbon materials, oxides, sulfides and nitrides may be used in combination, and may be crystalline or amorphous.
These carbon materials, oxides, sulfides, and nitrides are mainly carried on a negative electrode current collector and used as an electrode (negative electrode).

{Conductive material}
The conductive material is added to the electrode mixture when the electron conductivity and ionic conductivity of the electrode are not sufficient. In particular, since the positive electrode active material has low electronic conductivity, it is preferable to add a conductive material to the positive electrode mixture in order to increase the electronic conductivity of the electrode for a secondary battery. Further, when a high rate characteristic is required as a characteristic of the secondary battery, a conductive material is added to the electrode mixture in order to increase the ionic conductivity of the electrode used in the secondary battery.

A carbon material is used as the conductive material.
Examples of the carbon material include graphite powder, carbon black (for example, acetylene black), and fibrous carbon material (for example, graphitized carbon fiber, carbon nanotube).
By increasing the proportion of the conductive material in the electrode, the electron conductivity and ion conductivity of the electrode are increased, and charge / discharge efficiency and rate characteristics can be improved. If the ratio of the conductive material in the electrode is too high, the adhesion between the electrode mixture and the positive electrode current collector may be reduced, and the internal resistance may be increased. Usually, the ratio of the conductive material in the electrode mixture is 1 to 20 parts by weight with respect to 100 parts by weight of the active material.
The conductive material may be a single material or may be composed of a plurality of materials. In particular, when the electronic conductivity of the active material is not sufficient, it is preferable to combine the active material and the conductive material.

 When a conductive material is included in the secondary battery paint, the viscosity of the secondary battery paint increases and the shear rate dependency of the viscosity increases, and the coating property of the secondary battery paint is adjusted in the stirring step. It becomes more important. In particular, when the conductive material is carbon black, the viscosity of the secondary battery paint becomes higher and the shear rate dependency of the viscosity becomes larger. It becomes more important to adjust with.

{binder}
A thermoplastic resin is used as the binder.
Specific examples of the thermoplastic resin include polyvinylidene fluoride (hereinafter sometimes referred to as “PVdF”), polytetrafluoroethylene (hereinafter sometimes referred to as “PTFE”), and tetrafluoroethylene.・ Fluorine resin such as hexafluoropropylene / vinylidene fluoride copolymer, hexafluoropropylene / vinylidene fluoride copolymer and tetrafluoroethylene / perfluorovinyl ether copolymer; polyolefin such as polyethylene and polypropylene Resin; styrene-butadiene copolymer (hereinafter sometimes referred to as “SBR”). These thermoplastic resins are used alone or in combination of two or more.
In addition, a fluororesin and a polyolefin resin are used as a binder, and the positive electrode is so formed that the proportion of the fluororesin is 1 to 10 wt% and the proportion of the polyolefin resin is 0.1 to 2 wt% in 100 wt% of the positive electrode mixture By including a fluororesin and a polyolefin resin in the composite, a positive electrode composite having excellent adhesion to the positive electrode current collector can be obtained.

<Production process of secondary battery electrode>
The manufacturing process of the secondary battery electrode is a process of manufacturing the secondary battery electrode.
The production process of the secondary battery electrode generally includes a production process, a coating process, and a drying process of the secondary battery paint. The manufacturing process of the secondary battery electrode may further include a press step, a heat treatment process, and the like.

[Process for producing secondary battery paint]
The production process of the secondary battery paint is a process of producing the secondary battery paint, and includes a mixing process and a stirring process.
The mixing step and the stirring step are performed sequentially or simultaneously. Moreover, it is preferable to perform a mixing process and a stirring process sequentially, and it is more preferable to perform a stirring process after performing a mixing process.

{Mixing process}
The mixing step is a step of preparing a slurry by adding an active material, a conductive material, a binder and the like to a solvent and mixing them.

{Stirring step}
The stirring step is a step of preparing a secondary battery paint by stirring the slurry composed of a solvent, an active material, a conductive material, a binder and the like obtained in the mixing step.
In the stirring step, the slurry is stirred to prepare a secondary battery paint having more uniform particle dispersibility. By using a coating material for a secondary battery having sufficiently high particle dispersibility, there will be no coating defects such as rubbing in the coating process, and there will be no electrode cracking in the drying process. For secondary batteries obtained by using a coating for secondary batteries, that an electrode having a uniform film thickness distribution can be obtained, that an electrode having sufficient adhesion between the electrode mixture and the current collector can be obtained. In the secondary battery manufactured using the electrode, an effect that the function as a battery can be sufficiently exhibited is obtained.

 In particular, when a secondary battery electrode including an active material or conductive material having a small particle diameter and a large surface area is produced, it is preferable to obtain sufficient particle dispersibility in the secondary battery paint. When a material with a small particle size and a large surface area is included as a constituent material of the paint, the particles are highly cohesive. Therefore, in order to separate the particles in the stirring step, a large shear force is applied to a fine space. It is preferable. In order to give a large shearing force to the slurry in the stirring step, it is preferable to expose the slurry to a large shearing rate of stirring.

(Agitation shear rate)
The shearing speed of stirring is a speed gradient to which the slurry is exposed in the stirring process of the secondary battery paint, and is represented by the following formula (1).

By making the stirring shear rate 3 times or more larger than the maximum value of the coating shear rate described later, a coating material for a secondary battery having good coating property without causing poor coating can be obtained. Preferably, the shear rate of stirring is increased by 5 times or more, more preferably, the shear rate of stirring is increased by 10 times or more.
Further, in order to increase the peel strength between a layer made of an electrode mixture (hereinafter sometimes referred to as “electrode mixture layer”) and the current collector, the shear rate of stirring is 7500 S ⁻¹ or more. Is more preferable, and more preferably 10,000 S ⁻¹ or more.

"Agitation speed"
In the stirring process of the secondary battery coating material, the difference between the maximum value and the minimum value of the flow rate of the slurry is defined as the stirring speed in a certain flow direction at the portion where the slurry receives a shearing force.

"Agitation interval"
The agitation interval is an interval between two points on a line perpendicular to a certain flow direction in the portion where the slurry is subjected to a shearing force in the agitation process, and in particular, the slurry in the flow direction. This is the distance between the point at which the speed is maximum and the point at which the speed is minimum.

(Stirring method)
Examples of the stirring method used in the stirring step include an impeller turning method, a blade turning method, a turning thin film method, a rotor / stator mixer method, a colloid mill method, and a high-pressure homogenizer method.
In the stirring step, a plurality of stirring methods may be performed in order, or a plurality of stirring methods may be used simultaneously.

"Agitation process by impeller turning method"
The impeller swirling method is a stirring method in which the impeller (blade) is swung at a high speed inside a container containing a paint, and the shear stress generated by the paint flowing at a high speed in the vicinity of the impeller is used for stirring the paint.
As a stirring device using the impeller swirl method, for example, Dispermat (manufactured by VAM-GEZTMANN), T.M. K. Homo disperse (manufactured by Primix) can be mentioned.
In the impeller turning method, the maximum peripheral speed of the impeller is set as the stirring speed.
Further, in the impeller turning method, the flow rate of the paint contacting the impeller becomes the maximum value. The interval from the impeller to the point where the flow rate of the paint becomes 0 m · s ^{−1 in the} direction perpendicular to the rotation direction is defined as the stirring interval.

"Stirring process by blade rotation method"
In the blade swirl method, one or more blades are swirled inside the container containing the paint, and the shear stress caused by the paint flowing in the gap between the bottom and side surfaces of the container and the blade, This is a stirring method in which the shear stress generated by the flow of the paint in the gaps between them is used to stir the paint.
Examples of the stirring device using the blade turning method include T.W. K. Hibismix (Primix), T. K. Hibis Disper Mix (Primix), T. K. A combination mix (manufactured by PRIMIX) is mentioned.
In the blade turning method, for the shear stress generated in the gap between the blade and the bottom or side surface of the container, the maximum peripheral speed of the blade is set as the stirring speed. Regarding the shear stress generated in the gap between the blades in the blade turning method, the stirring speed is set to twice the maximum peripheral speed of the blade.
Regarding the shear stress generated in the gap between the blade and the bottom and side surfaces of the container in the blade turning method, the minimum value of the distance from the bottom and side surfaces of the container to the blade is set as the stirring interval. Regarding the shear stress generated in the gap between the blades in the blade turning method, the minimum value of the distance between the blades taken in the turning between the blades is set as the stirring interval.

"Agitating process by the rotating thin film method"
The swirling thin film method uses a stirrer that consists of a cylindrical container in which paint is placed and a wheel that rotates at high speed while maintaining a certain distance between the container and the paint flows in the gap between the container and the wheel. This is a stirring method in which the shear stress generated by this is used to stir the paint.
Examples of the stirring device using the rotating thin film method include a film mix (manufactured by Primics).
In the rotating thin film method, the maximum peripheral speed of the wheel is set as the stirring speed.
In the rotating thin film method, the minimum value of the distance between the side surface of the container and the wheel is set as the stirring interval.

"Agitating process by rotor / stator mixer method"
The rotor / stator mixer method uses a stirrer that is composed of a stator and a rotor that rotates at a high speed while maintaining a constant distance from the stator in the paint. This is a stirring method in which shear stress generated by flowing is used for stirring the paint.
As a stirring device using a rotor / stator type mixer method, for example, T.M. K. Examples include homomixer (manufactured by Primix), ultra tarax (manufactured by IKA), and silverson mixer (manufactured by Silverson).
In the rotor / stator mixer method, the maximum peripheral speed of the rotor is set as the stirring speed.
In the rotor / stator mixer method, the minimum interval between the rotor and the stator is set as the agitation interval.

"Stirring process by colloid mill method"
The colloid mill method uses a stirrer composed of a fixed disk and a fixed ring in a paint and a disk and a rotor that rotates at high speed while maintaining a fixed distance from the fixed disk and the fixed ring. In addition, the shearing stress generated by the coating material flowing in a narrow gap maintained between the stationary ring and the disk or rotor is used for stirring the coating material.
Examples of the stirring device using the colloid mill method include T.I. K. Examples include Mycoloyder (manufactured by Primix), Charlotte Colloidmill (manufactured by Chemicoloid Laboratories), and KORUMA Colloidmill (manufactured by Flyma Koruma).
In the colloid mill method, the maximum peripheral speed of the disk or rotor is set as the stirring speed.
In the colloid mill method, the minimum distance between the fixed disk or stationary ring and the disk or rotor is set as the stirring interval.

"Agitating process by high-pressure homogenizer method"
The high-pressure homogenizer method uses a high-pressure pump and an orifice mechanism (a mechanism with holes) to push the paint at a high pressure into a narrow gap in the orifice, and to quickly reduce the shear stress generated when the paint passes through the gap. This is a stirring method used for stirring.
Examples of the stirring device using the high-pressure homogenizer method include a homogenizer (manufactured by Sanwa Engineering Co., Ltd.) and a starburst (manufactured by Sugino Machine Co., Ltd.).
In the high-pressure homogenizer method, the maximum flow rate when the paint passes through the orifice is set as the stirring speed.
In the high-pressure homogenizer method, half the minimum value of the slit interval in the orifice through which the paint passes is set as the stirring interval.

[Coating process]
A coating process is a process of apply | coating the coating material for secondary batteries to a collector.
In the coating process, if the secondary battery paint is exposed to a higher shear rate than it can withstand, the continuous flow of the secondary battery paint is interrupted, which causes coating defects such as rubbing. . Therefore, it is preferable that the secondary battery paint can maintain a continuous flow even when exposed to a high shear rate in the coating process.

{Coating shear rate}
The coating shear rate is a speed gradient to which the secondary battery paint is exposed in the coating process of the secondary battery paint, and is represented by the following formula (2).

Shear rate of the coating, the maximum value is less than or equal 1/3 times the shear rate of the agitation described above is preferably 1500s ^-1 or more, 3000 s ^-1 or more is more preferable.

(Coating speed)
The coating speed is the maximum speed at which the secondary battery paint passes through the portion where the secondary battery paint undergoes a shearing action in the coating process.

(Coating interval)
The coating interval is the interval between two points on the straight line perpendicular to the flow direction in which the secondary battery paint reaches the maximum flow velocity at the portion where the secondary battery paint undergoes a shearing action in the coating process. Yes, the interval between the point at which the flow rate of the coating material for the secondary battery is the maximum value and the point at which the flow rate is the minimum value.

{Coating method}
Coating methods used in the coating process include reverse roll coating method, forward rotation roll coating method (direct roll coating method), kiss coating method, gravure coating method and other roll coating methods, curtain coating method (flow coating method). Fountain coating method (die coating method), blade coating method, knife coating method, rod coating method.
In the coating process, a plurality of coating methods may be used in combination.

"Coating process by roll coating method"
The roll coating method is a coating method using a mechanism for transferring paint to the surface of the roll and a mechanism for transferring paint attached to the surface of the roll to another part. As the roll coating method, the secondary battery paint adhered to the surface of the roll is brought into contact with the current collector, and the secondary battery paint is transferred from the roll to the current collector. And a coating method using a mechanism for laminating a secondary battery paint on a current collector and a coating method using a mechanism for transferring the secondary battery paint from a roll to a roll. In particular, when using a gravure roll whose surface is subjected to uneven engraving, it is called a gravure coating method.
Examples of the roll coating method include a reverse roll coating method, a forward rotating roll coating method (direct roll coating method), a kiss coating method, and a gravure coating method. In the roll coating method, between rolls and between a roll and a current collector. The coating is subjected to a shearing action. Between the rolls, the maximum value of the peripheral speed difference between the rolls is defined as the coating speed. Between the roll and the current collector, the maximum value of the speed difference between the roll and the current collector is defined as the coating speed.
In the roll coating method, the paint undergoes a shearing action between the rolls and between the roll and the current collector. Between the rolls, the minimum distance between the rolls is defined as the coating interval. Between the roll and the current collector, the minimum distance between the roll and the current collector is used as the coating interval.

"Coating process by curtain coating method (flow coating method)"
The curtain coating method is a coating method using a mechanism in which a paint extruded through an orifice flows down from a nozzle and is applied to a current collector that is an object to be coated.
In the curtain coating method, the paint undergoes a shearing action in the orifice. The maximum value of the speed of the paint passing through the orifice is defined as the coating speed.
In the curtain coating method, the paint undergoes a shearing action in the orifice. One half of the minimum slit interval at the orifice is defined as the coating interval.

"Coating process by fountain coating method (die coating method)"
The fountain coating method is a coating method that uses a mechanism that supplies a paint to an orifice, pressurizes and pushes the paint in the orifice, and applies it to a current collector that is an object to be coated.
Examples of the fountain coating method (die coating method) include a slot die coating method.
In the fountain coating method (die coating method), the paint is subjected to a shearing action in the orifice and in the application portion between the orifice and the current collector. In the orifice, the maximum value of the speed of the paint passing through the orifice is set as the coating speed. In the coating portion, the current carrying speed of the current collector is the coating speed.
In the fountain coating method (die coating method), the paint is subjected to a shearing action in the orifice and in the application portion between the orifice and the current collector. In the orifice, one half of the minimum slit interval in the orifice is set as the coating interval. In the coating portion, the interval between the orifice and the current collector is set as the coating interval.

"Coating process by blade coating method"
The blade coating method is a coating method that uses a blade mechanism that is a blade-like component that scrapes off excess paint adhering to a current collector or roll as a coating body to obtain a desired coating amount.
The blade coating method includes a method of moving the blade itself and a method of moving the object to be coated and the roll to which the extra paint is adhered while fixing the blade.
In the blade coating method, the paint undergoes a shearing action between the blade and the current collector. The maximum value of the speed difference between the blade and the current collector is defined as the coating speed.
In the blade coating method, the paint undergoes a shearing action between the blade and the current collector. The minimum distance between the blade and the current collector is the coating interval.

"Coating process by knife coating method"
The knife coating method uses a knife, which is a metal plate with a sharp tip, to scrape off excess paint adhering to a current collector or roll as a coating body and to use a mechanism that obtains a desired coating amount. It is a construction method.
In the knife coating method, there are a method of moving the knife itself and a method of moving the object to be coated with surplus paint adhered by fixing the knife.
In the knife coating method, the paint undergoes a shearing action between the knife and the current collector. The maximum value of the speed difference between the knife and current collector is taken as the coating speed.
In the knife coating method, the paint undergoes a shearing action between the knife and the current collector. The minimum distance between the knife and the current collector is the coating interval.

"Coating process by rod coating method"
The rod coating method is a mechanism that uses a stainless steel wire or piano wire wound around a rod to scrape off the excess paint adhering to the current collector or roll as the object to be coated to obtain the desired coating amount. Is a coating method using
In the rod coating method, the paint undergoes a shearing action between the rod and the current collector. The maximum value of the speed difference between the rod and current collector is defined as the coating speed.
In the rod coating method, the paint undergoes a shearing action between the rod and the current collector. The minimum distance between the rod and the current collector is the coating interval.

[Drying process]
The drying step is a step of preparing an unpressed electrode by fixing (deteriorating) the solvent contained in the coating material for the secondary battery applied to the current collector to fix the electrode mixture on the current collector. is there.

[Pressing process]
The pressing step is a step of pressing a non-pressed electrode to obtain a pressed electrode.
The pressing step is performed in order to adjust the density and porosity of the electrode mixture fixed on the current collector. By increasing the density of the electrode mixture, the electron conductivity in the electrode mixture is increased. Further, by increasing the adhesion between the electrode mixture and the current collector, the electrode strength is increased, and the peel strength of the electrode is increased.
Examples of the pressing method include a roll pressing method in which an unpressed electrode is passed through a gap between pressurized rolls to press the electrode.

[Heat treatment process]
The heat treatment step is a step of obtaining a secondary battery electrode by heat-treating the press electrode.
The heat treatment step is performed for the purpose of completely drying (completely removing) the residual solvent in the electrode mixture, alleviating the residual stress of the electrode, and improving the adhesion of the electrode mixture to the current collector.
In the heat treatment step, the press electrode is preferably heated under a reduced pressure atmosphere.
The temperature of the heat treatment is appropriately determined according to the type and composition of the solvent, active material, conductive material, binder, etc. constituting the secondary battery paint. The temperature of the heat treatment is usually in the range of 80 to 250 ° C.
The heat treatment time is usually in the range of 1 minute to 24 hours.

 EXAMPLES Hereinafter, although an Example and a comparative example demonstrate this invention further more concretely, this invention is not limited to a following example.

 The composition analysis method for the active material constituting the secondary battery paint, the crystal structure measurement method, the specific surface area measurement method and the average primary particle diameter measurement method, the secondary battery paint viscosity measurement method, The measuring method of the peeling strength of the electrode compound-material layer formed on the electric body is shown.

(1) Composition analysis After the active material is dissolved in hydrochloric acid, an inductively coupled plasma emission spectrometer (SPS3000, manufactured by SII NanoTechnology Co., Ltd.) (hereinafter sometimes referred to as “ICP-AES”) is used. The composition of the active material was analyzed.

(2) Measurement of crystal structure by powder X-ray diffraction method For measurement of the crystal structure of the active material, a powder X-ray diffraction measurement apparatus (RINT 2500 TTR type, manufactured by Rigaku Corporation) was used.
A CuKα radiation source was used as the X-ray radiation source.
The active material was filled in a dedicated holder and performed in the diffraction angle range of 2θ = 10 to 90 ° to obtain a powder X-ray diffraction pattern.

(3) Measurement of specific surface area After 0.5 g of active material was dried at 150 ° C. for 15 minutes in a nitrogen atmosphere, a BET specific surface area was measured using a BET specific surface area measuring device (Flowsorb II 2300, manufactured by Micromeritics). Was measured.
The BET specific surface area measured by the above method was defined as the specific surface area of the active material.

(4) Measurement of average primary particle diameter by SEM observation A particulate active material is placed on a conductive sheet pasted on a sample stage, and a scanning electron microscope (JSM-5510, manufactured by JEOL Ltd.) (hereinafter referred to as “SEM”). SEM observation was performed by irradiating an electron beam with an acceleration voltage of 20 kV.
The average primary particle diameter of the active material was measured by arbitrarily extracting 50 primary particles from an image (SEM photograph) obtained by SEM observation, measuring each particle diameter, and calculating the average value. .

(5) Viscosity measurement A rheometer (Rheometer AR550, manufactured by TA Instruments Inc.) was used to measure the viscosity of the coating material for secondary batteries.
The rheology of the secondary battery paint was measured at 23 ° C. using a stainless steel 4 ° cone with a diameter of 40 mm.
The viscosity at a shear rate of 3 s ^{−1 was taken as} the viscosity of the secondary battery paint.

(6) Measurement of peel strength A secondary battery electrode composed of a current collector and an electrode mixture layer formed on the current collector is cut into a width of 25 mm and a length of 100 mm, and an electrode mixture layer The glass epoxy plate (glass epoxy copper-clad laminate MCL-E-67, manufactured by Mejika Kasei Kogyo Co., Ltd.) and a 25 mm wide double-sided adhesive tape (Nystack strong double-sided tape NW-K25, manufactured by Nichiban Co., Ltd.) Fixed.
The current collector is peeled off from the electrode mixture layer from one end of the electrode, the glass epoxy plate is fixed to the lower part of the vertical tensile strength tester (Autograph DSS-500, manufactured by Shimadzu Corporation), and the current collector is fixed to the upper part did.
The tensile strength (N) of the electrode mixture of the secondary battery electrode and the current collector was measured by a 180 ° peel test in which the current collector was pulled upward at a pulling speed of 100 mm / min.
From the tensile strength (N) and the electrode width (25 mm), the peel strength (N / m) between the electrode mixture and the current collector was calculated.

"Example 1, comparative example 1"
<Preparation of secondary battery electrode>
[Process for producing secondary battery paint]
In Example 1 and Comparative Example 1, a secondary battery paint was prepared by the method described below.

{Mixing process}
A slurry was prepared by adding a positive electrode material, a conductive material and a binder to the solvent and mixing them.
NMP was used as the solvent.
As a positive electrode material, the composition is LiNi _0.47 Mn _0.48 Fe _0.05 O ₂ , the crystal structure is R-3m, the BET specific surface area is 10 m ² · g ⁻¹ , and the average primary particle diameter The one having a thickness of 200 nm was used.
As the conductive material, acetylene black (Denka Black HS100, manufactured by Denki Kagaku Kogyo Co., Ltd.) was used. The acetylene black had a BET specific surface area of 40 m ² · g ⁻¹ and an average primary particle size of 50 nm.
As the binder, PVdF (PVdF # 7300, manufactured by Kureha) was used.
In the slurry, the slurry was prepared so that the total ratio (solid content concentration) of the positive electrode material, the conductive material, and the binder in the total weight of the secondary battery paint was 50 wt%.
The weight ratios of the positive electrode material, the conductive material, and the binder constituting the electrode mixture were 90 wt%, 5 wt%, and 5 wt%, respectively.
100 mL of the mixture obtained by adding the positive electrode material, the conductive material and the binder to the solvent at a predetermined ratio was put in a stainless steel beaker having a diameter of 5 cm.
Using a disper mat (VAM-GEZTMANN, manufactured by GMBH) equipped with a toothed disk type impeller having a diameter of 4 cm, the impeller was rotated at a rotation speed of 1000 rpm and stirred for 10 minutes to prepare a slurry.
In the mixing step, the stirring speed was 2.1 m · s ⁻¹ . Further, the stirring interval was 0.005 m. That is, the shear rate of stirring was 420 s ⁻¹ .

{Stirring step}
In the slurry agitation step, a film mix 56-50 type (manufactured by Primix Co., Ltd.), which is an agitation device by a revolving thin film method in which a wheel is swirled in a paint placed in a container, was used.
In this stirrer, the slurry was subjected to a shearing action in the gap between the container (inner diameter 60 mm) and the wheel rotating inside (outer diameter 56 mm).
The stirring interval in this stirring device was 2 mm, which is the interval between the container and the wheel. The slurry is sheared by rotating the wheel inside the fixed container. By adjusting the peripheral speed of the wheel, the shear rate of stirring can be changed.
90 mL of the slurry obtained in the mixing step was placed in a film mix type 56-50 (manufactured by Primex), and the wheel was rotated at a peripheral speed of 6 m · s ⁻¹ and stirred for 180 s.
In the stirring step, the stirring speed was 6 m · s ⁻¹ . Further, the stirring interval was 0.002 m. That is, the shear rate of stirring was 3000 s ⁻¹ .
The viscosity of the obtained paint for secondary batteries was 38 Pa · s.

[Coating process]
The secondary battery paint was applied on an aluminum foil having a thickness of 20 μm.
At this time, a doctor blade type applicator (film applicator SA-204 with a micrometer, manufactured by Tester Sangyo Co., Ltd.) that can be adjusted to any coating interval, and an applicator (auto film applicator P1-1210, that can be adjusted to any coating speed) Tester Sangyo Co., Ltd.).
The distance between the blade and the aluminum foil was defined as the coating interval, and the coating speed was defined as the coating speed.

[Drying process]
The aluminum foil coated with the secondary battery coating material was placed in a hot air dryer (hot air dryer HT330K, manufactured by Enomoto Kasei Co., Ltd.) set at a temperature of 60 ° C. and dried to prepare an unpressed electrode.

[Pressing process]
In the pressing step, a small roll press (small desktop roll press SA-602 (load adjustment type), manufactured by Tester Sangyo Co., Ltd.) was used.
The electrode conveyance speed was 0.2 m · min ⁻¹ . The press pressure was adjusted so that the electrode density was 2.6 g / cm ³ .

[Heating process]
In the heating process, an electrode (press electrode) that had been subjected to the pressing process was placed in a vacuum dryer, and was allowed to stand at 150 ° C. for 8 hours in a vacuum to produce a secondary battery electrode.

<Evaluation of coatability>
The coating property when the coating for a secondary battery was applied at an arbitrary coating interval and an arbitrary coating speed was evaluated.
In the coating process, there was no occurrence of rubbing or streaking, and when the current collector was not exposed in the unpressed electrode, the coating property was good (◯).
In the coating process, rubbing and streaking occurred, and when there was a portion where the current collector was exposed in the unpressed electrode, the coating property was judged as poor (Δ).
Table 1 shows the stirring conditions, coating conditions, and coating properties in Example 1 and Comparative Example 1.

 From the results shown in Table 1, good coatability was obtained when the shear rate of stirring was 3 times or more larger than the shear rate of coating.

"Example 2, comparative example 2"
<Preparation of secondary battery electrode>
[Process for producing secondary battery paint]
In Example 2 and Comparative Example 2, a secondary battery paint was produced by the method described below.

{Mixing process}
A slurry was prepared in the same manner as in Example 1.

{Stirring step}
In the same manner as in Example 1, a film mixing type 56-50 (manufactured by Primics), which is a stirring device, was used.
90 mL of the slurry obtained in the mixing step was put into a film mix type 56-50 (manufactured by Primix), and the wheel was rotated at a peripheral speed of 15 m · s ⁻¹ and stirred for 180 s.
In the stirring step, the stirring speed was 15 m · s ⁻¹ . Further, the stirring interval was 0.002 m. That is, the shear rate of stirring was 7500 s ⁻¹ .
The viscosity of the obtained paint for secondary batteries was 12 Pa · s.

[Coating process]
The coating process was performed in the same manner as in Example 1.
[Drying process]
A drying step was performed in the same manner as in Example 1.
[Pressing process]
The pressing process was performed in the same manner as in Example 1.
[Heating process]
The heating process was performed in the same manner as in Example 1.

<Evaluation of coatability>
In the same manner as in Example 1, the coatability of the secondary battery paint was evaluated.
Table 2 shows the stirring conditions, coating conditions, and coating properties in Example 2 and Comparative Example 2.

 From the results of Table 2, good coating properties were obtained when the stirring shear rate was 3 times or more larger than the coating shear rate.

"Example 3, comparative example 3"
<Preparation of secondary battery electrode>
[Process for producing secondary battery paint]
In Example 3 and Comparative Example 3, a secondary battery paint was prepared by the method described below.

{Mixing process}
A slurry was prepared in the same manner as in Example 1.

{Stirring step}
In the same manner as in Example 1, a film mixing type 56-50 (manufactured by Primics), which is a stirring device, was used.
90 mL of the slurry obtained in the mixing step was put into a film mix type 56-50 (manufactured by Primex), and the wheel was rotated at a peripheral speed of 30 m · s ⁻¹ and stirred for 180 s.
In the stirring step, the stirring speed was 30 m · s ⁻¹ . Further, the stirring interval was 0.002 m. That is, the shear rate of stirring was 15000 s ⁻¹ .
The viscosity of the obtained paint for secondary batteries was 10 Pa · s.

[Coating process]
The coating process was performed in the same manner as in Example 1.
[Drying process]
A drying step was performed in the same manner as in Example 1.
[Pressing process]
The pressing process was performed in the same manner as in Example 1.
[Heating process]
The heating process was performed in the same manner as in Example 1.

<Evaluation of coatability>
In the same manner as in Example 1, the coatability of the secondary battery paint was evaluated.
Table 3 shows the stirring conditions, coating conditions, and coating properties in Example 3 and Comparative Example 3.

 From the results of Table 3, good coating properties were obtained when the stirring shear rate was 3 times or more larger than the shear rate of coating.

<Evaluation of peel strength>
Secondary battery paints were produced under different stirring conditions, and peel strength was measured for unpressed electrodes produced under the same coating conditions. Tables 4 and 5 show the measurement results.

From the results of Table 4 and Table 5, by setting the shear rate of stirring to 7500 s ⁻¹ or more, in addition to obtaining good coatability, a secondary battery electrode having high peel strength was obtained. .

According to the method for producing a secondary battery electrode of the present invention, it is possible to produce a secondary battery electrode that is stable and mass-productive without causing poor coating of the secondary battery paint. Moreover, since the obtained electrode for secondary batteries has high peel strength of the electrode mixture layer, it has excellent electrode structure stability and battery performance, and is therefore industrially promising.

Claims (13)

A mixing step of preparing a slurry by mixing an active material, a binder, and a solvent;
An agitation step of agitating the slurry to prepare a secondary battery paint;
A method for producing an electrode for a secondary battery comprising: applying a coating for the secondary battery to a current collector;
In the stirring step, the slurry is stirred at a shear rate of 3 times or more than the maximum shear rate at which the secondary battery paint is exposed in the coating step. . The manufacturing method of the electrode for secondary batteries of Claim ¹ whose maximum shear rate exposed by the said coating process is 1500 s < ^-1 > or more.  The manufacturing method of the electrode for secondary batteries of Claim 1 or 2 with which the said slurry contains a electrically conductive material further.  The manufacturing method of the electrode for secondary batteries of any one of Claims 1-3 whose particle diameter of the said active material is 0.005-5 micrometers. The manufacturing method of the electrode for secondary batteries of any one of Claims 1-4 whose specific surface area of the said active material is 5-100 m < ² > / g.  The manufacturing method of the electrode for secondary batteries of any one of Claims 1-5 whose transition metal element which comprises the said active material is at least 1 sort (s) chosen from the group which consists of manganese, nickel, and cobalt.  The manufacturing method of the electrode for secondary batteries of any one of Claims 1-6 whose crystal structure of the said active material is a layered structure.  The manufacturing method of the electrode for secondary batteries of any one of Claims 3-7 in which the said electrically conductive material contains carbon black.  The manufacturing method of the electrode for secondary batteries of any one of Claims 1-8 using the stirring apparatus stirred by the turning thin film method in the said stirring process. The manufacturing method of the electrode for secondary batteries of any one of Claims 1-9 whose shear rate which stirs the said slurry is 7500 s < ^-1 > or more. A mixing step of preparing a slurry by mixing an active material, a binder, and a solvent;
Stirring the slurry to prepare a secondary battery paint, and a method for producing a secondary battery paint comprising:
In the stirring step, the slurry is stirred at a shear rate of 3 times or more than the maximum shear rate at which the secondary battery paint is exposed in the coating step. Method.  11. A secondary battery electrode manufactured by the method for manufacturing a secondary battery electrode according to claim 1. A secondary battery comprising the secondary battery electrode according to claim 12.