JP5471591B2 - Conductive composition for electrode - Google Patents

Description

The present invention relates to a conductive composition used for producing an electrode constituting a secondary battery and a capacitor. In particular, the conductive composition for an electrode of the present invention can be used for a lithium secondary battery, a nickel hydride secondary battery, a fuel cell, a capacitor and the like, but is particularly suitable for use in a lithium ion secondary battery and a lithium ion capacitor. It is.
Further, the present invention provides a lithium having an electrode having excellent discharge characteristics or charge characteristics at a large current, cycle characteristics, and conductivity of the electrode mixture layer, and having a small contact resistance between the electrode current collector and the electrode mixture layer. The present invention relates to a secondary battery.

  In recent years, small portable electronic devices such as digital cameras and mobile phones have been widely used. These electronic devices have always been required to minimize the volume and reduce the weight, and the batteries to be mounted are also required to be small, light, and have a large capacity. Further, in large-sized secondary batteries for use in automobiles or the like, it is desired to realize a large non-aqueous electrolyte secondary battery instead of a conventional lead-acid battery.

  In order to meet such demands, lithium secondary batteries are being actively developed. As an electrode of a lithium secondary battery, a positive electrode in which an electrode mixture composed of a positive electrode active material containing lithium ions, a conductive additive, an organic binder, and the like is fixed to the surface of a current collector of a metal foil, and lithium ion removal A negative electrode is used in which an electrode mixture composed of an insertable negative electrode active material, a conductive additive, an organic binder, and the like is fixed to the surface of a metal foil current collector.

  In general, lithium transition metal composite oxides such as lithium cobaltate and lithium manganate are used as the positive electrode active material, but these have low electronic conductivity and have sufficient battery performance when used alone. I can't get it. Therefore, attempts have been made to improve the conductivity by reducing the internal resistance of the electrode by adding a carbon material such as carbon black (for example, acetylene black) as a conductive additive. In particular, reducing the internal resistance of the electrode is very important in enabling discharge with a large current and improving charge and discharge efficiency.

  On the other hand, graphite (graphite) is usually used as the negative electrode active material. Although graphite itself has conductivity, it is known that charge and discharge characteristics are improved by adding carbon black such as acetylene black as a conductive aid together with graphite. This is because the graphite particles generally used are large, so if graphite alone is used, the gap when filled in the electrode layer will increase. However, when carbon black is used as a conductive additive, fine carbon black is used. It seems that the contact area increases by filling the gaps between the graphite particles and the resistance decreases. However, in this case as well, the conductive effect is reduced if the dispersion of the conductive aid is insufficient.

  In this way, reducing the internal resistance of the electrode is one of the very important factors in enabling discharge with a large current and improving the efficiency of charge and discharge.

  However, carbon materials with excellent electrical conductivity (conducting aids) have a strong cohesive force due to their large structure and specific surface area, making it difficult to uniformly mix and disperse in the electrode mixture forming slurry of lithium secondary batteries. is there. And, when the dispersibility and particle size control of the carbon material that is the conductive auxiliary agent are insufficient, the internal resistance of the electrode cannot be reduced because the uniform conductive network is not formed, and as a result, the lithium that is the active material There has been a problem that the performance of transition metal composite oxides, graphite and the like cannot be sufficiently extracted. In addition, if the dispersion of the conductive additive in the electrode mixture is insufficient, resistance distribution occurs on the electrode plate due to partial aggregation, current concentrates when used as a battery, and partial heat generation occurs. In addition, problems such as accelerated deterioration may occur.

  In addition, when forming an electrode mixture layer on an electrode current collector such as a metal foil, repeated charging and discharging a large number of times, the interface between the current collector and the electrode mixture layer, and the active material inside the electrode mixture layer There is a problem that the adhesion at the interface of the conductive auxiliary agent is deteriorated and the battery performance is lowered. This is because the active material and the electrode mixture layer repeatedly expand and contract due to the lithium ion doping and dedoping during charging and discharging, so that the electrode mixture layer and the current collector interface and the active material and conductive auxiliary agent interface are localized. This is thought to be due to the generation of shear stress and the deterioration of interfacial adhesion. In this case as well, if the dispersion of the conductive additive is insufficient, the adhesion reduction becomes significant. This is considered to be because when coarse agglomerated particles are present, the stress is hardly relaxed.

  In addition, as a problem between the electrode current collector and the electrode mixture, for example, when aluminum is used as the positive electrode current collector, an insulating oxide film is formed on this surface, and the contact between the electrode current collector and the electrode mixture There is also a problem that resistance increases.

  Several proposals have been made for the problems between the electrode current collector and the electrode mixture as described above. For example, Patent Document 1 and Patent Document 2 attempt to form a coating film in which a conductive agent such as carbon black is dispersed on the collector electrode as an electrode underlayer. In this case, too, the conductive agent is dispersed. If it is bad, sufficient effect cannot be obtained.

  In lithium secondary batteries, dispersion of a carbon material that is a conductive additive is one of the important points. Patent Documents 3 and 4 describe examples in which a surfactant is used as a dispersant when carbon black is dispersed in a solvent. However, since the surfactant has a weak adsorption force on the surface of the carbon material, it is necessary to increase the amount of the surfactant added in order to obtain good dispersion stability. As a result, the amount of the active material that can be contained Decreases and the battery capacity decreases. Further, if the surfactant is not sufficiently adsorbed on the carbon material, the carbon material will aggregate. Further, a general surfactant has a remarkably low dispersion effect in an organic solvent as compared with dispersion in an aqueous solution.

  In Patent Document 5 and Patent Document 6, when carbon black is dispersed in a solvent or water, the dispersion state of the carbon slurry is improved by adding a dispersion resin, and the carbon slurry and the active material are mixed. And the method of producing the compound material for electrodes is disclosed. However, although this method improves the dispersibility of carbon black, a large amount of dispersed resin is required when dispersing fine carbon black having a large specific surface area, and a dispersed resin having a large molecular weight is carbon black. Since the surface is covered, the conductive network is hindered and the resistance of the electrode is increased, and as a result, the effect of improving the dispersion of carbon black may be offset.

  In addition to the improvement in the dispersibility of the electrode material, an important factor for improving the charge / discharge efficiency is an improvement in the wettability of the electrode with respect to the electrolytic solution. Since the electrode reaction occurs at the contact interface between the electrode material surface and the electrolytic solution, it is important that the electrolytic solution penetrates into the electrode and the electrode material is well wetted. As a method of promoting the electrode reaction, a method of increasing the surface area of the electrode by using a fine active material or a conductive auxiliary agent has been studied. There is a problem that it is difficult to improve battery performance because the contact area of the battery does not increase.

As a method for improving the wettability of an electrode, Patent Document 7 discloses a method of providing fine voids between active material particles by including carbon fibers having a fiber diameter of 1 to 1000 nm in an electrode. . However, since carbon fibers are usually intertwined in a complicated manner, uniform dispersion is difficult, and a uniform electrode cannot be produced simply by mixing carbon fibers. In addition, in this document, there is a method of using carbon fiber whose surface is oxidized for dispersion control. However, when carbon fiber is directly oxidized, the conductivity and strength of carbon fiber are reduced. There is a problem of end up. Patent Document 8 discloses a method for improving the wettability by adsorbing a surfactant such as a higher fatty acid alkali salt to a negative electrode material mainly composed of carbon powder. In particular, the agent often does not have sufficient dispersion performance in a non-aqueous system, and a uniform electrode coating film cannot be obtained. In these examples, the total performance including the dispersibility of the electrode material was insufficient.
JP 2000-123823 A Japanese Patent Laid-Open No. 2002-298753 JP-A-63-236258 JP-A-8-190912 Japanese Patent Laid-Open No. 2003-157846 JP-T-2006-51679 Japanese Patent Laying-Open No. 2005-063955 JP, 6-60877, A Moreover, as for an electric double layer capacitor, a symmetrical electrode capacitor which arranges a separator between two polarizable electrodes, and is impregnated with electrolyte is common. These are characterized in that they can be charged / discharged more rapidly than conventional secondary batteries, have high output density, and are less susceptible to repeated charging / discharging due to no chemical change.

Generally, an electrode for an electric double layer capacitor has a structure in which an electrode layer containing a carbonaceous material such as activated carbon is laminated on a current collector. The electrode layer is made of a carbonaceous material and a binder, and there are an extrusion rolling method and a coating method as a method for producing the electrode material.
As an electrode for an electric double layer capacitor, for example, in Reference 1, a slurry made of an aqueous solution of a binder such as activated carbon powder and carboxymethylcellulose is prepared, and a current collector such as an aluminum foil is applied to a current collector by a method such as roll coating and doctor blade coating. An electrode made by deposition is disclosed.

  Document 10 includes a dispersion containing one or more cellulose compounds selected from the group consisting of ammonium salt of carboxymethyl cellulose resin, polyvinyl alcohol, methyl cellulose, and hydroxypropyl cellulose resin, and a tetrafluoroethylene resin emulsion or latex. Further, there is disclosed a method in which a coating material in which activated carbon and a conductivity imparting agent are dispersed is applied on a conductive foil.

In addition to conventional capacitors, a power storage device called a hybrid capacitor has attracted attention. A hybrid capacitor is usually a so-called asymmetric electrode capacitor that uses a polarizable electrode for the positive electrode and a nonpolarizable electrode for the negative electrode. Further, the negative electrode is contacted with lithium metal, and lithium ions are preliminarily deposited by a chemical method or an electrochemical method. There have also been proposals intended to significantly increase the energy density by occlusion and support (doping). (References 11 to 12)
JP-A-3-280518 International Publication No. WO1998 / 058397 Japanese Patent Laid-Open No. 8-1007048 However, the techniques disclosed in Patent Documents 1 to 12 have various problems. That is, since the conductive material is not sufficiently dispersed, the direct current resistance and impedance are not sufficiently low, and when the electrode layer is formed by coating with electrode mixture ink, the conductive path that connects the electrode active material and the current collector However, it is not always satisfactory as a secondary battery and a capacitor, for example, the electric capacity decreases when charging / discharging is repeated.

  In addition, conductive materials having high conductivity generally have a strong chain structure “structure”, but the impact force is too strong in the dispersion process in a bead mill or the like, so the “structure” is broken and the conductivity of the material is large. If the density is lowered or the bulk density is low, the dispersion will be insufficient and the solid content concentration will not increase, the energy to evaporate the solvent during drying will increase, the production efficiency will deteriorate, etc. It is not preferable.

  Furthermore, in an electrode mixture ink composed of an electrode active material, a binder, and a conductive material, since the dispersion to the electrode is insufficient, the coating on the electrode is not stable, and a suitable electrode film is not formed. There were problems such as product defects, such as peeling of the coating film from the current collector.

  The present invention has been made to solve the above-described conventional problems, and by using a granular conductive composition for an electrode using a conductive material having a specific bulk density and volume resistivity, Efficiently form conductive paths in the composite layer to produce electrodes with low electrical resistance, improve storage stability of the electrode mixture ink without impairing the conductivity of the conductive material, and improve coatability It aims at improving the performance of the secondary battery and capacitor which are produced using the conductive composition for electrodes of the present invention.

That is, the present invention
A conductive composition comprising a conductive material, a solvent, and a wetting improver,
The conductive material has a bulk density of 0.01 to 0.20 g / cm ³ and a volume resistivity of 0.001 to 0.1 Ω · cm (when the compression density is 0.9 g / cm ³ ).
The conductive composition is granular and has a solid content of 20 to 60% by weight.

In the present invention, the wetting improver is a compound having two or more polar functional groups per molecular unit, the conductive composition is granular, and the solid content is 25 to 55% by weight. It is related with the said electroconductive composition for electrodes characterized by these.
In the present invention, the wettability improver is a compound having two or more polar functional groups per molecular unit, and the wettability improver has a weight average molecular weight of 1,000 or less and / or a weight average molecular weight of 3 The electroconductive composition for electrodes is characterized by comprising a wetting improver B of 1,000 to 2,000,000.

In addition, the present invention relates to the conductive composition for an electrode, wherein the conductive material is at least one selected from the group consisting of acetylene black, furnace black, ketjen black, graphite, graphitized carbon, and fibrous carbon material.
The granular conductive composition has a bulk density of 0.30 to 0.80 g / cm ³ , and relates to the conductive composition for electrodes.
Further, the present invention relates to the conductive composition for an electrode, wherein the conductive composition is medialessly dispersed.
In addition, the present invention relates to the conductive composition for electrodes, wherein the conductive composition is subjected to high-speed shear dispersion with a stirring blade and / or a stirring blade.

Furthermore, it is related with the manufacturing method of the said electrically conductive composition for electrodes manufactured using the 1st process which wets a conductive material to a solvent with a wettability improvement agent, and the 2nd process of granulating the wetted conductive material.
The conductive material further comprises a first step of wetting the conductive material with a solvent with a wetting improver and a second step of granulating the wet conductive material, and the conductive material has a bulk density of 0.01 to 0.20 g / cm ^3. Volume resistivity 0.001 to 0.1 Ω · cm (when the compression density is 0.9 g / cm ³ ), granular and solid content is 20 to 60% by weight. The present invention relates to a method for producing a composition.

Furthermore, it is related with the electrode for positive electrodes or negative electrodes formed using the said electroconductive composition for electrodes.
Furthermore, it is related with the secondary battery formed using the said electrode for positive electrodes or negative electrodes.
Furthermore, it is related with the capacitor formed using the said electrode for positive electrodes or negative electrodes.

  According to a preferred embodiment of the present invention, since the conductive carbon material in the electrode layer is distributed evenly and the conductive carbon material is excellent in dispersion stability, the electrode active material and the current collector are preferably provided with a conductive path. A conductive composition for electrodes to be formed is obtained. Furthermore, by using the conductive composition for an electrode according to a preferred embodiment of the present invention for an electrode of a secondary battery, a capacitor, or a fuel cell, the adhesion between the current collector and the electrode composition, the electrode active material, The adhesion to the conductive carbon material and the wettability of the electrode composition with respect to the electrolytic solution are improved, and the internal resistance of the electrode can be reduced and the charge / discharge efficiency can be improved. The performance can be improved comprehensively.

  The conductive composition for an electrode of the present invention is preferably granular. The granular form means that the conductive carbon material is round, oval, dumpling or indefinite, even when it is round. When the conductive carbon material is granulated, the conductive component is distributed evenly in the mixture ink at the initial dispersion stage when the composition is added, and the composition is granular at the stage where the dispersion proceeds thereafter. Since the material is dissolved and adsorbed on the surface of the electrode active material, or the structure of the conductive material can be expanded in the binder, the conductive material does not bias the distribution of conductive components in the coating film when the electrode is manufactured. A path is formed. As a result, the resistance of the electrode is lowered, and the charge / discharge characteristics and load characteristics (rate characteristics) are remarkably improved, and an excellent battery is obtained. In addition, the dispersion and kneading time can be greatly shortened, and there is no scattering and much better handling than powdered conductive carbon materials, enabling efficient production and extremely effective in reducing the total cost. . On the other hand, when it is gel-like, when it is stored for a long period of time, gelation proceeds to form a cake and is inferior in handling properties. In addition, in the pasty form, the stability of the coating liquid is inferior, such as precipitation of the carbon material due to long-term storage, and since it contains a large amount of solvent, the viscosity at the time of forming a mixture ink becomes low and the degree of freedom in design becomes extremely low.

  The conductive composition for electrodes of the present invention preferably has a solid content of 20 to 60% by weight, more preferably 25 to 55% by weight. If it is within the above range, the viscosity of the mixture paste is high and the coating liquid is excellent in coating stability. Furthermore, the distribution of the conductive component in the electrode coating film is suitable, and the bias is reduced. No conductive path is formed, improving battery performance. On the other hand, when the solid content is 20% by weight or less, the shape cannot be maintained and handling is deteriorated. When the solid content is more than 60% by weight, it becomes a cause of unraveling failure when forming a composite paste, which causes a problem.

<Conductive carbon material as conductive aid>
The bulk density of the conductive material used in the present invention is preferably 0.01 to 0.20 g / cm ³ . If it is greater than 0.20 g / cm ³ , it is difficult to form a suitable conductive path in the electrode coating film, and the resistance of the electrode increases. If it is less than 0.01 g / cm ^3, it becomes too bulky and the electrode density is extremely lowered, making it unsuitable for practical use.
The conductive material in the present invention is most preferably a carbon material. The carbon material is not particularly limited as long as it is a conductive carbon material, but graphite, carbon black, carbon nanotube, carbon nanofiber, carbon fiber, fullerene, etc. alone or in combination of two or more. Can be used.
The volume resistivity of the conductive material used in the present invention is preferably 0.001 to 0.1 Ω · cm (when the compression density is 0.9 g / cm ³ ). If it exists in this range, since the resistivity of the electrode which is the effect of this invention will fall, the efficiency by charging / discharging becomes favorable.

  Carbon black is a furnace black produced by continuously pyrolyzing a gas or liquid raw material in a reactor, especially ketjen black using ethylene heavy oil as a raw material. Channel black rapidly cooled and precipitated, thermal black obtained by periodically repeating combustion and thermal decomposition using gas as a raw material, and various types such as acetylene black using acetylene gas as a raw material alone, Or two or more types can be used together. Ordinarily oxidized carbon black, hollow carbon and the like can also be used.

  The oxidation treatment of carbon is performed by treating carbon at a high temperature in the air or by secondary treatment with nitric acid, nitrogen dioxide, ozone, etc., for example, such as phenol group, quinone group, carboxyl group, carbonyl group. This is a treatment for directly introducing (covalently bonding) an oxygen-containing polar functional group to the carbon surface, and is generally performed to improve the dispersibility of carbon. However, since it is common for the conductivity of carbon to fall, so that the introduction amount of a functional group increases, it is preferable to use the carbon which has not been oxidized.

As the specific surface area of the carbon black used increases, the number of contact points between the carbon black particles increases, which is advantageous in reducing the internal resistance of the electrode. Specifically, the specific surface area (BET) determined from the amount of nitrogen adsorbed is 20 m ² / g or more and 1500 m ² / g or less, preferably 50 m ² / g or more and 1500 m ² / g or less, more preferably 100 m ^2. / G or more,
It is desirable to use a thing of 1500 m < ² > / g or less. If carbon black having a specific surface area of less than 20 m ² / g is used, it may be difficult to obtain sufficient conductivity, and carbon black of more than 1500 m ² / g may be difficult to obtain from commercially available materials. is there.

  Moreover, the particle size of the carbon black to be used is preferably 0.005 to 1 μm, and particularly preferably 0.01 to 0.2 μm in terms of primary particle size. However, the primary particle diameter here is an average of the particle diameters measured with an electron microscope or the like.

Examples of commercially available carbon black include
Furnace blacks manufactured by Tokai Carbon, such as Toka Black # 4300, # 4400, # 4500, and # 5500;
Furnace Black made by Degussa such as Printex L;
Furnace black manufactured by Colombian, such as Raven 7000, 5750, 5250, 5000 ULTRA III, 5000 ULTRA, Conductex SC ULTRA, 975 ULTRA, PUER BLACK100, 115, and 205;
# 2350, # 2400B, # 2600B, # 30050B, # 3030B, # 3230B, # 3350B, # 3400B, and # 5400B furnace black manufactured by Mitsubishi Chemical Corporation;
Furnace black from Cabot, such as MONARCH 1400, 1300, 900, Vulcan XC-72R, and Black Pearls 2000;
Furnace black manufactured by TIMCAL, such as Ensaco 250G, Ensaco 260G, Ensaco 350G, and SuperP-Li;
Ketjen Black EC-300J, EC-600JD and other Akzo Ketjen Black, and
Although acetylene black by Denki Kagaku Kogyo Co., Ltd., such as Denka Black, Denka Black HS-100, and FX-35, is mentioned, it is not limited to these.

  Examples of the graphite include natural graphite such as artificial graphite, flake graphite, lump graphite, and earth graphite, but they may be used in combination.

  As the conductive carbon fibers, those obtained by firing from petroleum-derived raw materials are preferable, but those obtained by firing from plant-derived raw materials can also be used. For example, VGCF manufactured by Showa Denko Co., Ltd. manufactured with petroleum-derived raw materials can be mentioned.

<Wetting improver>
The wetting improver enhances the wettability between the conductive carbon material and the solvent, and forms into a granule. At the same time, it dissolves the conductive carbon material quickly when forming a composite paste, and finally distributes the conductive component. It plays the role of forming a suitable conductive path in the electrode coating film.

  The wetting improver is not particularly limited as long as it is a compound having two or more polar functional groups per molecule unit and a lipophilic group. Lipophilic groups are effective in interaction with the carbon material surface, and two or more polar functional groups are effective in charge repulsion and solvent uptake, and the conductive composition is suitably distributed when used in composite pastes. It is thought to play a role. Among these, the wettability improver A has a molecular weight of 50 to 1000, so that the conductive carbon material can be adjusted in a relatively short time. The wettability improver B has a weight average molecular weight of 3000 to 2 million, so that it is granular. This contributes to the storage stability of the resulting conductive composition, and further to the storage stability of the composite paste. These wetting improvers may be used independently for A and B, respectively, and more preferably used together.

Examples of the wetting improver A having a molecular weight of 50 to 1000 or less include aliphatic compounds having basic functional groups, aromatic compounds having basic functional groups, organic dye derivatives having basic functional groups, and basic functional groups. One or more derivatives selected from the group consisting of an anthraquinone derivative having, an acridone derivative having a basic functional group, and a triazine derivative having a basic functional group, or an aliphatic compound having an acidic functional group, having an acidic functional group Examples thereof include one or more derivatives selected from the group consisting of aromatic compounds, organic dye derivatives having an acidic functional group, and triazine derivatives having an acidic functional group.
Furthermore, examples of the wetting improver B having a weight average molecular weight of 3000 to 2 million include a resin having a basic functional group, a resin having an acidic functional group, and a vinylamide resin.

  The resin having a basic functional group is composed of a vinyl polymer (C1) having two hydroxyl groups in one terminal region constituting the polymer (G1), and two hydroxyl groups and one thiol group in the molecule. A polymer having an amine value of 1 to 100 mgKOH / g obtained by radical polymerization of an ethylenically unsaturated monomer (c2) in the presence of the compound (c11), a single terminal region constituting the polymer (G2) The polymer (C2) having 1 or 2 (meth) acryloyl groups in the polymer is a vinyl polymer, or a polymer containing an amine value of 1 to 100 mg KOH / g, including polyester, polyvinyl, polyurethane, polyester , Polyethers, formalin condensates, silicones, and composite polymers thereof. Furthermore, two or more kinds of resins having these basic functional groups can be used in combination.

<Other resins having basic functional groups>
Although it does not specifically limit as resin which has a commercially available basic functional group, For example, the following are mentioned.

  As the resin having a basic functional group manufactured by Big Chemie, Disperbyk-108, 109, 112, 116, 130, 161, 162, 163, 164, 166, 167, 168, 180, 182, 183, 184, 185, 2000, 2001, 2050, 2070, 2150, or BYK-9077.

  As a resin having a basic functional group manufactured by Nippon Lubrizol, SOLPERSE 9000, 13240, 13650, 13940, 17000, 18000, 19000, 20000, 24000SC, 24000GR, 28000, 31845, 32000, 32500, 32600, 33500, 34750, 35100, 35200, 37500, 38500, or 39000.

  As a resin having a basic functional group manufactured by Efka Additives, EFKA4008, 4009, 4010, 4015, 4020, 4046, 4047, 4050, 4055, 4060, 4080, 4300, 4330, 4400, 4401, 4402, 4403 4406, 4500, 4550, 4560, 4570, 4580, or 4800.

Examples of the resin having a basic functional group manufactured by Ajinomoto Fine-Techno Co., Ltd. include Ajisper PB711, Azisper PB821, or Azisper PB822.
HKM-150A and HFB-150A are mentioned as resin which has a basic functional group made by Nippon Oil & Fats.
Examples of the resin having a basic functional group manufactured by Enomoto Kasei Co., Ltd. include Disparon 1850, 1860, or DA-1401.

Examples of the resin having a basic functional group manufactured by Kyoeisha Chemical include Floren DOPA-15B and Floren DOPA-17.
As an acidic resin, two hydroxyl groups at one end are formed by radical polymerization of an ethylenically unsaturated monomer (m) in the presence of a compound (s) having two hydroxyl groups and one thiol group in the molecule. A polyvinyl resin (C2) obtained by reacting a hydroxyl group in the vinyl polymer (c) with an acid anhydride group in the tetracarboxylic dianhydride (d), and
The following general formula (1):
^{_{(HOOC-) m -R 21 - (}} - COO - [- R 23 -COO-] n -R 22) t (1)
[In General Formula (1), R ²¹ is a tetravalent tetracarboxylic acid compound residue, R ²² is a monoalcohol residue, R ²³ is a lactone residue, and m is 2 or 3, n is an integer from 1 to 50, and t is (4-m). ]
There is a polyester resin (C3) represented by

  The resin having an acidic functional group is not limited to the above three types, but other than the three types, polyvinyl type, polyurethane type, polyester type, polyether type, formalin condensate, silicone type, and these And a composite polymer. Furthermore, two or more kinds of resins having these acidic functional groups can be used in combination.

<Other resins having acidic functional groups>
Although it does not specifically limit as resin which has a commercially available acidic functional group, For example, the following are mentioned.

  As resin having an acidic functional group manufactured by Big Chemie, Anti-Terra-U, U100, 203, 204, 205, Disperbyk-101, 102, 106, 107, 110, 111, 140, 142, 170, 171, 174 , 180, 2001, BYK-P104, P104S, P105, 9076, or 220S.

Examples of the resin having an acidic functional group manufactured by Nippon Lubrizol include SOLPERSE 3000, 21000, 26000, 36000, 36600, 41000, 41090, 43000, 44000, or 53095.
Examples of the resin having an acidic functional group manufactured by Efka Additives include EFKA4510, 4530, 5010, 5044, 5244, 5054, 5055, 5063, 5064, 5065, 5066, 5070, and 5071.

Examples of the resin having an acidic functional group manufactured by Ajinomoto Fine Techno Co. include Ajisper PN411 or Azisper PA111.
Examples of the resin having an acidic functional group manufactured by ELEMENTIS include Nuosperse FX-504, 600, 605, FA620, 2008, FA-196, or FA-601.
Examples of the resin having an acidic functional group manufactured by Lion Corporation include Politi A-550 or Politi PS-1900.

As resins having an acidic functional group manufactured by Enomoto Kasei Co., Ltd., Disparon 2150, KS-860, KS-873SN, 1831, 1860, PW-36, DA-1200, DA-703-50, DA-7301, DA-325 , DA-375, or DA-234.
Examples of resins having acidic functional groups manufactured by BASF Japan include JONCRYL 67, 678, 586, 611, 680, 682, 683, 690, 52J, 57J, 60J, 61J, 62J, 63J, 70J, HPD-96J, 501J, 354J. , 6610, PDX-6102B, 7100, 390, 711, 511, 7001, 741, 450, 840, 74J, HRC-1645J, 734, 852, 7600, 775, 537J, 1535, PDX-7630, 352J, 252D, 538J7640 7641, 631, 790, 780, or 7610.

Examples of the resin having an acidic functional group manufactured by Mitsubishi Rayon include Dianal BR-60, 64, 73, 77, 79, 83, 87, 88, 90, 93, 102, 106, 113, or 116.
Examples of the resin having an acidic functional group manufactured by NOF Corporation include AKM-0531, AFB-1521, AAB-0851, and AWS-0851.

There are carboxymethyl cellulose and its sodium salt, ammonium salt and modified products. For example, as resins made by Daicel Finechem, CMC Daicel 1220, 1230, 1240, 1250, 1260, 1330, 1350, 1360, 1380, 1390, 2200, 2260, 2280, 2450 and the like.
The vinylamide resin is not particularly limited, and examples thereof include polyvinylacetamide, polyacrylamide, polyvinylpyrrolidone, alkylated polyvinylpyrrolidone, a polyvinylpyrrolidone graft copolymer, and a copolymer of vinylpyrrolidone and a comonomer.

  Comonomers that can be copolymerized with vinylpyrrolidone include α-olefin, vinyl acetate, ethyl acrylate, methyl acrylate, methyl methacrylate, dimethylaminoethyl methacrylate, acrylamide, methacrylamide, acrylonitrile, ethylene, styrene, maleic anhydride, Examples include acrylic acid, sodium vinyl sulfate, vinyl chloride, vinyl pyrrolidine, trimethylsiloxy vinyl silane, vinyl propionate, vinyl caprolactam, and methyl vinyl ketone.

  In addition, an acid-modified product obtained by treating the vinylamide resin with an organic acid or an inorganic acid may be used.

Among the vinylamide resins, in particular, treatment with a substantially neutral vinylamide resin such as polyvinylpyrrolidone, vinylpyrrolidone-1-butene copolymer, or vinylpyrrolidone-styrene copolymer, or an organic acid or an inorganic acid. An acid-modified product of polyvinyl pyrrolidone is preferably used.

  The addition amount of the wetting improver is determined by the specific surface area of the carbon material as the conductive aid used. Generally, the wetting improver is 0.5 parts by weight or more and 40 parts by weight or less, preferably 1 part by weight or more and 35 parts by weight or less, more preferably 2 parts by weight or more, with respect to 100 parts by weight of the carbon material. Add up to 30 parts by weight. If the addition amount is small, a sufficient wettability improving effect cannot be obtained, and adding too much is not preferable because it causes a decrease in battery performance.

<Positive electrode active material>
The positive electrode active material for producing the composite paste using the conductive composition of the present invention is not particularly limited, but metal compounds such as metal oxides and metal sulfides that can be doped or intercalated with lithium ions Can be used. Examples thereof include transition metal oxides such as Ti, Fe, Co, Ni, and Mn, composite oxides of the transition metal and lithium, and inorganic compounds such as sulfides of the transition metal.
In particular,
Transition metal oxide powders such as MnO, V ₂ O ₅ , V ₆ O ₁₃ , and TiO ₂ ;
A composite oxide powder of lithium and a transition metal, such as lithium nickelate, lithium cobaltate, lithium manganate having a layered structure, and lithium manganate having a spinel structure;
Lithium iron phosphate which is a phosphate compound having an olivine structure, lithium manganese phosphate, one having a nasicon structure, a polyanionic material; and
Transition metal sulfide powders such as TiS ₂ and FeS;
Is mentioned.
In addition, two or more of the above inorganic compounds may be mixed and used.

As the specific surface area of the positive electrode active material used increases, the number of contact points between the positive electrode active material particles increases, which is advantageous in reducing the internal resistance of the positive electrode. Specifically, the specific surface area (BET) determined from the amount of nitrogen adsorption is 0.1 m ² / g or more and 150 m ² / g or less, preferably 1 m ² / g or more and 120 m ² / g or less, more preferably 1.5 m ² / g or more, it is desirable to use the following 100 m ² / g. When a positive electrode active material having a specific surface area of less than 0.1 m ² / g is used, it may be difficult to obtain sufficient conductivity, and a positive electrode active material having a specific surface area of more than 150 m ² / g may not be easily manufactured. .

  In addition, the particle size of the positive electrode active material to be used is preferably 0.01 to 500 μm, particularly preferably 0.05 to 100 μm in terms of primary particle size. However, the primary particle diameter here is an average of the particle diameters measured with an electron microscope or the like.

Among positive electrode active materials, lithium iron phosphate having an olivine structure is a preferable material from the viewpoints of cost and safety.
Since lithium iron phosphate having a simple olivine structure has very low electronic conductivity compared to lithium cobaltate or the like, it is difficult to obtain excellent battery characteristics. Therefore, in order to improve the electron conductivity, a method is adopted in which a conductive material such as a carbon material is supported on the particles or the primary particle diameter is reduced.
The carbon material-supported lithium iron phosphate is not particularly limited, but can be produced with reference to Japanese Patent Application Laid-Open Nos. 2003-292308 and 2003-292309.

For example, ferrous phosphate octahydrate (Fe ₃ (PO ₄ ) ₂ · 8H ₂ O) and lithium phosphate (Li ₃ PO ₄ ) are used so that the element ratio of lithium to iron is 1: 1. And a carbon material (for example, acetylene black, ketjen black, etc.) that is a conductive substance, or an organic compound that is decomposed by firing to become a carbon material, and the carbon material component in the final product is 0. It is obtained by further adding 1 to 50% by weight, pulverizing and mixing with a dry pulverizer, etc., then firing at 600 ° C. for several hours in an inert gas atmosphere, and pulverizing the resulting fired product. It is done.

<Negative electrode active material>
The negative electrode active material used in the present invention is not particularly limited as long as it can be doped or intercalated with lithium ions. For example, metal Li, alloys thereof such as tin alloy, silicon alloy, lead alloy, Li _X Fe ₂ O ₃ , Li _X Fe ₃ O ₄ , Li _X WO ₂ , lithium titanate, lithium vanadate, silicon Metal oxides such as lithium oxide, conductive polymers such as polyacetylene and poly-p-phenylene, amorphous carbonaceous materials such as soft carbon and hard carbon, artificial graphite such as highly graphitized carbon materials, or natural Examples thereof include carbonaceous powders such as graphite, carbon black, mesophase carbon black, resin-fired carbon materials, air-growth carbon fibers, and carbon fibers.

  These negative electrode active materials can be used alone or in combination.

  As the negative electrode active material used in the present invention, a composite material made of a conductive material is also preferably used. Examples of the conductive substance include a carbon material, a conductive polymer material, a metal, and the like. In consideration of the interaction with the dispersant of the present invention, a carbon material or a conductive polymer material is preferable.

  Examples of the conductive polymer material include polyaniline, polypyrrole, polythiophene, and polyphenylene derivatives. Carbonaceous materials include graphite such as natural graphite (scale-like graphite), artificial graphite, expanded graphite, etc., acetylene black, ketjen black, channel black, furnace black, lamp black as amorphous carbon, Carbon blacks such as thermal black, and carbon nanotubes, carbon nanofibers and the like are mentioned as fibrous carbon materials. Examples of the metal include Al, Ti, Fe, Ni, Cu, Zn, Ag, and Sn.

  These complexing processes may be performed in combination of a plurality as required.

  As a method of compositing the negative electrode active material with a conductive material, for example, in the case of compositing a carbon material and a metal, mechanofusion, hybridization treatment and the like described in JP-A No. 2003-308845, Japanese Patent No. 3985263, etc. In the case of compounding a conductive polymer material and a conductive polymer material, a method of dipping in an organic solvent solution in which a conductive polymer is dissolved as described in JP-A-2001-68096, followed by drying and heat treatment Etc. Furthermore, a thermal decomposition product coating method of an organic substance by a CVD method, a formation method of a coating layer on an active material surface using a plasma method, and the like are also included. As other methods for coating the surface of the active material particles with a conductive material, a method using a binder and surface adsorption using frictional charging generated when powders dispersed in a gas phase come into contact with each other are used. The method of performing etc. can also be used.

  In addition, for metal-based, metal oxide-based negative electrode active materials, or metal-based negative electrode active materials, coupling with a silane coupling agent or the like in consideration of the interaction with the wetting improver used in the present invention. It is also possible to treat the surface with an agent.

<Solvent>
Examples of the solvent used in the present invention include alcohols, glycols, cellosolves, amino alcohols, amines, ketones, carboxylic acid amides, phosphoric acid amides, sulfoxides, carboxylic acid esters, and phosphoric acid. Examples include esters, ethers, nitriles, and water.
In order to obtain the solubility of the binder resin component and the dispersion stability of the conductive material as the conductive auxiliary agent, it is preferable to use a highly polar solvent.
For example, amide solvents such as water, alcohol, N, N-dimethylformamide, N, N-diethylformamide, N, N-dimethylacetamide, N, N-diethylacetamide, etc., N-methyl Examples include, but are not limited to, pyrrolidone, hexamethylphosphoric triamide, and dimethyl sulfoxide. Two or more types can be used in combination.

<Binder>
Examples of the binder for producing a composite ink using the conductive composition of the present invention include acrylic resin, polyurethane resin, polyester resin, phenol resin, epoxy resin, phenoxy resin, urea resin, melamine resin, alkyd resin, acrylic resin. Examples thereof include resin, formaldehyde resin, silicon resin, fluororesin, cellulose resin such as carboxymethylcellulose, synthetic rubber such as styrene-butadiene rubber and fluororubber, and conductive resin such as polyaniline and polyacetylene. Moreover, the modified body, mixture, aqueous emulsion, or copolymer of these resin may be sufficient.
Specifically, ethylene, propylene, vinyl chloride, vinyl acetate, vinyl alcohol, maleic acid, acrylic acid, acrylic ester, methacrylic acid, methacrylic ester, acrylonitrile, styrene, vinyl butyral, vinyl acetal, vinyl pyrrolidone, etc. Examples thereof include a copolymer contained as a structural unit.
From the viewpoint of resistance, it is preferable to use a polymer compound having a fluorine atom in the molecule, such as polyvinylidene fluoride, polyvinyl fluoride, and polytetrafluoroethylene.

  Moreover, as for the weight average molecular weight of these resin as a binder, 10,000-1,000,000 are preferable. When the molecular weight is small, the resistance of the binder may decrease. When the molecular weight is increased, the resistance of the binder is improved, but the viscosity of the binder itself is increased, the workability is lowered, and it acts as an aggregating agent.

<Positive electrode mixture ink for lithium secondary battery>
The conductive composition for an electrode of the present invention can be used by adding to a positive electrode mixture ink for a lithium secondary battery. When used as a positive electrode mixture ink, it contains a conductive composition treated with the above wetting improver, a positive electrode active material, a solvent, and a binder component, and is used as a positive electrode mixture ink. It is preferable.
The proportion of the positive electrode active material in the total solid content in the positive electrode mixture ink is desirably 80% by weight or more and 98.5% by weight or less, preferably 83% by weight or more and 95% by weight or less. If the proportion of the positive electrode active material is less than 80% by weight, it may be difficult to obtain sufficient electrical conductivity and discharge capacity. If the proportion exceeds 98.5% by weight, the proportion of the binder component decreases, and thus current collection. Adhesion to the body may be reduced, and the positive electrode active material may be easily detached.
Further, the ratio of the solid content of the carbon material as the conductive auxiliary agent in the total solid content in the positive electrode mixture ink is 0.5% by weight or more and 19% by weight or less, preferably 1.0% by weight or more and 15% by weight. It is desirable to use at less than%. When the ratio of the carbon material as the conductive auxiliary agent is less than 0.5% by weight, it may be difficult to obtain sufficient conductivity. When the proportion exceeds 19% by weight, the positive electrode active material that greatly contributes to battery performance. As a result, a problem such as a decrease in discharge capacity may occur.

Further, the ratio of the binder component in the total solid content in the positive electrode mixture ink is preferably 1% by weight or more and 10% by weight or less, and preferably 2% by weight or more and 8% by weight or less. When the ratio of the binder component is less than 1% by weight, the binding property is lowered, and thus the positive electrode active material and the carbon material as the conductive auxiliary agent may be easily detached from the current collector, which exceeds 10% by weight. And, since the ratio of the positive electrode active material and the carbon material as the conductive auxiliary agent is decreased, the battery performance may be decreased.
The proper viscosity of the positive electrode mixture ink depends on the method of applying the positive electrode mixture ink, but generally it is preferably 100 mPa · s or more and 30,000 mPa · s or less.

The conductive composition of the present invention preferably has a bulk density of 0.30 to 0.80 g / cm ³ . The reason is that the composition of the present invention is granular and has a solid content concentration of 20 to 60%. Therefore, if it is in the above bulk density range, the initial dispersion stage in which the composition is added at the time of forming the composite ink. In the mixed ink, the conductive component is distributed evenly, and at the stage of subsequent dispersion, the granular composition is dissolved and adsorbed on the surface of the electrode active material, or the structure of the conductive material can be expanded in the binder. It can be confirmed that this is a suitable state. When the electrode is produced, a conductive path is formed in which the conductive material is not biased in the distribution of the conductive component in the coating film. As a result, the charge / discharge characteristics and load characteristics (rate characteristics) are remarkably improved by reducing the resistance of the electrodes, and not only lithium ion batteries but also lithium ion capacitors, electric double layer capacitors, fuel cells, etc. as excellent electrodes Can be used for In addition, the dispersion and kneading time can be greatly shortened, and there is no scattering and much better handling than powdered conductive carbon materials, enabling efficient production and extremely effective in reducing the total cost. .

  Medialess dispersion is suitable for obtaining the conductive composition of the present invention. Normally, a bead mill or the like is used in the slurry preparation process. However, in a dispersion method using a medium such as beads or balls, it is difficult to achieve a solid content concentration of 20% or more, and the structure of the conductive material in the slurry. Is easily destroyed. When the structure of the conductive material is broken and cut, not only is the conductivity significantly reduced, but the bulk density of the conductive material is increased, and the resistance of the electrode is increased by cutting or narrowing the conductive path of the electrode layer. The function as a battery is reduced.

  In order to obtain high battery performance, it is required to distribute the conductive material and form a suitable conductive path while maintaining the structure of the conductive material as described above. At that time, in order to suitably form a conductive path connecting the electrode active material and the current collector, the conductive material is deaggregated, adsorbed on the surface of the active material, and further passed through the binder between the active materials, and then the conductive material. It is necessary to create a network with an expanded structure. For this reason, it is important to perform medialess dispersion in the step of obtaining granules by dispersing a conductive material and a wetting improver in a liquid component. In the medialess dispersion, the collision between the conductive material and the medium does not occur, so that the structure of the conductive material can be maintained and the conductivity can be expressed. However, a twin-screw extruder such as an extruder or an apparatus that destroys the structure of a conductive carbon material such as KCK is excluded from the medialess disperser of the present invention. Among the medialess dispersions, dispersion by jet flow or high-speed shearing with stirring blades and stirring blades is particularly preferable. By this high-speed shearing dispersion, the structure of the conductive material is hardly destroyed, and it becomes easy to obtain a highly conductive electrode.

As a dispersion apparatus that performs medialess dispersion, for example, a high-speed rotary shearing type apparatus, a high-speed rotation type apparatus using a centrifugal field, and the like are known. For example,
Mixers such as dispersers, homomixers, or planetary mixers;
"Henschel mixer" manufactured by Mitsui Mining Co., Ltd. "Super mixer" manufactured by Kawata Co., Ltd. "Trimix" manufactured by Inoue Seisakusho, "Dissolver", "BDM 2-axis mixer", "PD mixer", "CDM concentric mixer", M Technique Homogenizers such as “Clairemix” manufactured by Co., Ltd., “Intelligent Mixer” manufactured by Eirich, or “Fillmix” manufactured by PRIMIX
Wet jet mill (genus “Genus PY”, Sugino Machine “Starburst”, Nanomizer “Nanomizer”, etc.) M Technic “Claire SS-5”, or Nara Machinery “MICROS” Medialess dispersers such as; or
Other examples include, but are not limited to, kneaders, roll mills such as two rolls and three rolls. Further, as the disperser, it is preferable to use a disperser that has been subjected to a metal mixing prevention treatment from the disperser.

  In the present invention, dispersion by high-speed rotational shearing is suitable for improving the granular content and solid content concentration. As the high-speed rotary shearing type disperser used, those equipped with a stirring blade and / or a stirring blade are preferable. A high-speed shearing disperser equipped with stirring blades and / or stirring blades applies mechanical shearing force continuously to the stirring blades and / or stirring blades that rotate at high speed to suitably solve the agglomerated conductive material, and finally to strong stirring. The composition can be formed into granules by the action. When such a high-speed shear disperser is used, a battery and a capacitor excellent in battery performance can be suitably obtained.

  The high-speed disperser including the stirring blade and / or stirring blade used in the present invention is preferably a multistage stirring blade and / or a multistage stirring blade. Furthermore, the stirring blade and / or the stirring blade can take various shapes depending on the type of active material, conductive material, binder, etc., and the blade or blade may be bent, elliptical, disc-shaped, or cylindrical, in order to increase the stirring efficiency. The shape is not particularly limited. High-speed dispersers include a horizontal axis type and a vertical axis type. Examples of the horizontal axis type include a turbulizer, a sand turbo, a paddle mixer, a complex, and a paste mixer. , Speed mixers, power kneaders, rigid mixers, hybrid mixers, dispersive agitators, twin shaft mixers, combimixes, flow jet mixers, etc., but the vertical type is preferably super mixer (Kawata), Henschel mixer Representative examples include Mitsui Mine / Henschel Germany) and “Intelligent Mixer” manufactured by Eirich.

  In the high-speed disperser of the present invention, the rotation speed of the stirring blade and / or the stirring blade is preferably 500 to 6000 rpm, particularly preferably 1000 to 5000 rpm. If it is less than 500 rpm, it becomes difficult for the wetting improver or solvent to wet the surface without being biased to the conductive material, and if it exceeds 6000 rpm, it may cause heat generation to cause decomposition of the wetting improver or aggregation of the conductive material. It is not preferable.

  Moreover, also when using a roll mill, it is preferable to use a ceramic roll. Only one type of dispersion device may be used, or a plurality of types of devices may be used in combination.

  Furthermore, if necessary, the conductive composition of the present invention can be granulated by a granulator if necessary in addition to the above dispersion kneader. Examples thereof include a rolling fluidized coating apparatus (multiplex), a fluidized bed granulator / dryer, a stirring granulator (vertical granulator), and a crushing granulator.

  The method for producing a conductive composition of the present invention comprises a first step of wetting the conductive carbon material with a solvent with a wetting improver, and a second step of granulating the wet conductive carbon material. And a suitable conductive composition having a solid content of 25 to 60% by weight is obtained. By passing through the first step, it becomes possible to unravel the aggregated carbon material while improving the wettability of the conductive carbon material with the solvent. Furthermore, the carbon material clarified in the second step incorporates a solvent through a wetting improver, and a granular composition is obtained that is easy to handle and easily forms a conductive path in the electrode coating.

EXAMPLES Hereinafter, although this invention is demonstrated in more detail based on an Example, this invention is not limited to an Example. In the examples, “parts” represents “parts by weight” and “%” represents “% by weight”. The dispersed particle size of the electrode active material dispersion and the electrode mixture paste was determined by determination using Microtrac UPA-EX150 (manufactured by Nikkiso) or a grind gauge (according to JIS K5600-2-5). Further, the viscosity of the electrode active material dispersion and the conductive auxiliary agent dispersion was measured with an E type viscometer (“RE80 type viscometer” manufactured by Toki Sangyo Co., Ltd.) at 25 ° C. at a rotation speed of 50 rpm.
Further, the bulk density of the granular conductive composition can be measured in accordance with the method described in JIS-R1628. It can be determined from the weight when placed in a 100 cm ³ container.

<Preparation of conductive composition for electrode>
[Electroconductive compositions for electrodes (1) to (21)]
35 parts of acetylene black (Denka black powder, bulk density 0.04 g / cm ³ , volume resistivity 0.05 Ω · cm; compression density 0.9 g / cm ³ , manufactured by Denki Kagaku Kogyo Co., Ltd.) serving as a conductive aid Preparation of 0.7 part of the derivative (A) having a basic functional group and 64.7 parts of N-methyl-2-pyrrolidone (NMP), and a high-speed shearing treatment at 2000 rpm with a supermixer give a granular and solid content of 35 0.7% (35% by weight of carbon) of the electrode conductive composition (1) was obtained.

  In the same manner, wetting improvers and conductive materials shown in Tables 1 to 4 were added and dispersed with a medialess disperser to obtain a granular conductive composition (solid content 20 to 60%). Table 5 shows the composition table. In addition, the electroconductive composition (14) for electrodes is granulated (pill shape) using a stirring granulator (vertical granulator) after dispersing the dispersion. Table 6 shows the storage stability, handling properties, composite ink processability, and electrode resistance evaluation results of the obtained conductive composition.

[Comparison (1) to (5)]
In comparisons 1 to 5, since the conductive material having a specific bulk density and volume resistivity required for the present invention, and a wetting improver are not used, the obtained conductive composition has a granular and high concentration solid content. It turns out that the thing of cannot be obtained. Table 5 shows the composition table. Table 6 shows the storage stability, handling properties, composite ink processability, and electrode property evaluation results of the obtained conductive composition.

In comparison 2, the composition is prepared with an extruder (double-screw extruder PCM30; manufactured by Ikekai Tekko Co., Ltd.), but it is necessary to increase the binder component in order to sufficiently disperse the conductive material, which lowers the electrode conductivity. Cause it. On the other hand, when the binder component is reduced and dispersed, the structure of the conductive material is destroyed by the compression shear of the screw, and the electrode conductivity is also lowered.
In Comparative 3, media dispersion using a bead mill is carried out for 10 hours. However, even if the dispersion time is increased, the solid content concentration is limited to 20%, and the shape of the composition becomes the boundary between the paste and the gel, and the conductive composition The processability and handling of the product are significantly reduced. Furthermore, as the bead dispersion time increases, the structure of the conductive material is promoted, causing a decrease in electrode conductivity.
In Comparative 4, bead mill dispersion was performed using a surfactant (Syntrex EH-R; 2-ethylhexyl-sulfuric acid ester sodium salt, manufactured by NOF Corporation) instead of the wetting improver. It can be seen that the storage stability of the coating liquid is inferior to the use of the agent.
In Comparative 5, media dispersion by a bead mill was performed for 5 hours, and a composition having a solid content concentration of 15% was obtained. Since the paste is in a liquid form, handling properties are good, but long-term storage of 6 months has a problem that the conductive material is settled and stirring must be performed as appropriate. Further, as the bead dispersion time increases, the structure of the conductive material is promoted, causing a problem in that the electrode conductivity is lowered.

<Conductive material>
<Carbon black>
-Denka Black HS-100 (manufactured by Denki Kagaku Kogyo Co., Ltd.):
Acetylene black, bulk density 0.15 g / ml, volume resistivity 0.05 Ωcm.
・ Denka black powder product (manufactured by Denki Kagaku Kogyo):
Acetylene black, bulk density 0.04 g / ml, volume resistivity 0.05 Ωcm.
・ Denka Black FX-35 (manufactured by Denki Kagaku Kogyo Co., Ltd.):
Acetylene black, bulk density 0.05 g / ml, volume resistivity 0.03 Ωcm.

-Talker Black # 5500 (manufactured by Tokai Carbon Co., Ltd.):
Furnace black, bulk density 0.05 g / ml, volume resistivity 0.05 Ωcm.
Super-P Li (manufactured by TIMCAL):
Conductive carbon, bulk density 0.16 g / ml, volume resistivity 0.03 Ωcm.
-KS-6 (manufactured by TIMCAL):
Graphite, bulk density 0.07 g / ml, volume resistivity 0.02 Ωcm.

-PURE BLACK 205 (Colombia):
Graphitized carbon, bulk density 0.30 g / ml, volume resistivity 0.07 Ωcm.
-EC-300J (manufactured by Akzo):
Ketjen black, bulk density 0.10 g / ml, volume resistivity 0.01 Ωcm.

・ VGCF (manufactured by Showa Denko):
Carbon nanofiber (CNF), bulk density 0.15 g / ml, volume resistivity 0.004 Ωcm, fiber length 10-20 μm, fiber diameter 150 nm, specific surface area 13 m ² / g.

・ CNT:
Carbon nanotube, bulk density 0.01 g / ml, volume resistivity 0.004 Ωcm, fiber length 5-40 μm, fiber diameter 40-80 nm, specific surface area 25 m ² / g

<Wetting improver>
The wetting improver A is shown below. The molecular weight is preferably 50 to 1000.

<Derivatives (A) to (H) having basic functional groups>
-Dye derivatives having basic functional groups: (A), (B), (C), (H)
Anthraquinone derivatives having basic functional groups: (F)
Acridone derivatives having basic functional groups: (G)
Triazine derivatives having basic functional groups: (D), (E)
<Derivatives (I) to (P) having acidic functional groups>
-Pigment derivatives having acidic functional groups: (J), (M), (N), (O)
Triazine derivatives having acidic functional groups: (I), (J) (K), (L), (P)

  Next, wetting improver B is shown below. A weight average molecular weight of 3000 or more and 2 million or less is preferable.

<Resin having an acidic functional group>
AKM-053 (manufactured by NOF Corporation): weight average molecular weight of about 3,000 to 100,000 <resin having basic functional group>
Azisper PB821 (manufactured by Ajinomoto Fine Techno): weight average molecular weight of about 3,000 to 100,000 <resin having two or more other polar functional groups>
CMC2200 (manufactured by Daicel Chemical Industries): weight average molecular weight of about 1 to 2 million

<Vinylamide resin>
・ Polyvinylpyrrolidone (A1-1)
ISP Japan PVP K-30; weight average molecular weight of about 300,000 alkylated polyvinylpyrrolidone (A1-2)
Agrimar AL-10LC made by ISP Japan
-Copolymer of N-vinyl-2-pyrrolidone and methyl methacrylate (A1-3)
-Copolymer of N-vinyl-2-pyrrolidone and N-vinylacetamide (A1-5)
・ Poly N-vinylacetamide (A2-1)
PNVA GE191 made by Showa Denko
-Copolymer of N-vinylacetamide and acrylonitrile (A2-2)
-Copolymer of N-vinylacetamide and acrylamide (A2-3)

[Preparation of copolymer of N-vinyl-2-pyrrolidone and methyl methacrylate (A1-3)]
A reaction vessel equipped with a gas introduction tube, a thermometer, a condenser, and a stirrer was charged with 80 parts of N-vinyl-2-pyrrolidone and 20 parts of methyl methacrylate and replaced with nitrogen gas. The inside of the reaction vessel was heated to 80 ° C., and a solution prepared by dissolving 0.1 part of 2,2′-azobisisobutyronitrile in 100 parts of N-methylpyrrolidone was dropped from the dropping tank over 2 hours, Thereafter, stirring was continued at the same temperature for 3 hours. It was confirmed that 95% or more had reacted by solid content measurement, and the reaction was terminated. Thus, a copolymer (A1-3) solution of N-vinyl-2-pyrrolidone and methyl methacrylate having a solid content of 50% was obtained. The weight average molecular weight (Mw) of the obtained vinylamide resin (A1-3) was 30000.

[Preparation of copolymer of N-vinyl-2-pyrrolidone and maleic acid (A1-4)]
A reaction vessel equipped with a gas introduction tube, a thermometer, a condenser, and a stirrer was charged with 80 parts of N-vinyl-2-pyrrolidone and 20 parts of maleic acid and replaced with nitrogen gas. The inside of the reaction vessel was heated to 80 ° C., and a solution prepared by dissolving 0.1 part of 2,2′-azobisisobutyronitrile in 100 parts of N-methylpyrrolidone was dropped from the dropping tank over 2 hours, Thereafter, stirring was continued at the same temperature for 3 hours. The solid content measurement confirmed that 95% or more had reacted, and the reaction was terminated. Thus, a copolymer (A1-4) solution of N-vinyl-2-pyrrolidone and maleic acid having a solid content of 50% was obtained. The weight average molecular weight (Mw) of the obtained vinylamide resin (A1-4) was 30000.

[Preparation of copolymer of N-vinyl-2-pyrrolidone and N-vinylacetamide (A1-5)]
A reaction vessel equipped with a gas introduction tube, a thermometer, a condenser, and a stirrer was charged with 50 parts of N-vinyl-2-pyrrolidone and 50 parts of N-vinylacetamide and replaced with nitrogen gas. The inside of the reaction vessel was heated to 80 ° C., and a solution prepared by dissolving 0.1 part of 2,2′-azobisisobutyronitrile in 100 parts of N-methylpyrrolidone was dropped from the dropping tank over 2 hours, Thereafter, stirring was continued at the same temperature for 3 hours. The solid content measurement confirmed that 95% or more had reacted, and the reaction was terminated. Thus, a copolymer (A1-5) solution of N-vinyl-2-pyrrolidone and N-vinylacetamide having a solid content of 50% was obtained. The weight average molecular weight (Mw) of the obtained vinylamide resin (A1-5) was 30000.

[Preparation of copolymer of N-vinylacetamide and acrylonitrile (A2-2)]
A reaction vessel equipped with a gas introduction tube, a thermometer, a condenser, and a stirrer was charged with 80 parts of N-vinyl-2-pyrrolidone and 20 parts of acrylonitrile and replaced with nitrogen gas. The inside of the reaction vessel was heated to 80 ° C., and a solution prepared by dissolving 0.1 part of 2,2′-azobisisobutyronitrile in 100 parts of N-methylpyrrolidone was dropped from the dropping tank over 2 hours, Thereafter, stirring was continued at the same temperature for 3 hours. The solid content measurement confirmed that 95% or more had reacted, and the reaction was terminated. Thus, a copolymer (A2-2) solution of N-vinylacetamide and acrylonitrile having a solid content of 50% was obtained. The weight average molecular weight (Mw) of the obtained vinylamide resin (A2-2) was 30000.

[Preparation of copolymer of N-vinylacetamide and acrylamide (A2-3)]
In a reaction vessel equipped with a gas introduction tube, a thermometer, a condenser, and a stirrer, 80 parts of N-vinyl-2-pyrrolidone and 20 parts of acrylamide were charged and replaced with nitrogen gas. The inside of the reaction vessel was heated to 80 ° C., and a solution prepared by dissolving 0.1 part of 2,2′-azobisisobutyronitrile in 100 parts of N-methylpyrrolidone was dropped from the dropping tank over 2 hours, Thereafter, stirring was continued at the same temperature for 3 hours. The solid content measurement confirmed that 95% or more had reacted, and the reaction was terminated. Thus, a copolymer (A2-3) solution of N-vinylacetamide and acrylamide having a solid content of 50% was obtained. The weight average molecular weight (Mw) of the obtained vinylamide resin (A2-3) was 30000.

<Electrode active material>
Activated carbon powder (“Fine activated carbon RP20” manufactured by Kuraray Chemical): average particle size 5.0 μm, specific surface area 2000 m ² / g.
Mesophase carbon (MCMB 6-28, manufactured by Osaka Gas Chemical Co.): average particle size 5
7 μm, specific surface area 4 m ² / g
<Binder>
KF polymer W # 1100 (manufactured by Kureha):
Polyvinylidene fluoride (PVDF), weight average molecular weight of about 280,000.
PTFE 30-J (Mitsui / DuPont Fluorochemicals):
60% polytetrafluoroethylene (PTFE) aqueous dispersion BM-400B (manufactured by Nippon Zeon):
40% styrene butadiene rubber (SBR) aqueous dispersion

<Dispersion evaluation of conductive composition for electrode>
Each conductive composition for electrodes is diluted with a solvent so that the solid content concentration becomes 10%, and the dispersed particle size is measured with Microtrac UPA-EX150 (manufactured by Nikkiso). “◯” was 1 μm or more and less than 5 μm, and “Δ” was 5 μm or more. Further, coarse agglomerated particles were measured with a grind gauge as required.
As for the viscosity, the viscosity of the electrode mixture ink and the conductive composition was measured with an E type viscometer (“RE80 type viscometer” manufactured by Toki Sangyo Co., Ltd.) at 25 ° C. at a rotation speed of 50 rpm.
Table 7 shows the results of evaluation of dispersion of the electrode conductive composition.

<Evaluation of storage stability of conductive composition for electrode>
Each electroconductive composition for electrodes was stored at room temperature for 6 months, and it was confirmed whether the shape before storage was retained and the cake was not solidified or whether the change in solid content was within 5%. Dilute to a solid content concentration of 10% with a solvent, and measure the viscosity at 25 ° C. at a rotational speed of 50 rpm with an E-type viscometer (“RE80 type viscometer” manufactured by Toki Sangyo Co., Ltd.). It was confirmed whether the viscosity increase was within 10% compared to the initial value. The case where there was no shape retention, solid content concentration change, and viscosity increase was evaluated as “◯”, and when all three items were not satisfied, it was evaluated as “X”. Table 6 shows the results.

<Evaluation of handling property of conductive composition for electrode and processability of composite ink>
In the process of converting the conductive composition for each electrode into a composite ink, “○” is satisfied when all two items are satisfied, such as whether the powder is scattered around at the time of preparation, or whether the preparation workability is easy, and “×” otherwise. The handling property was evaluated. Furthermore, when the conductive composition for each electrode is made into a composite ink using an active material, a binder and a solvent, the case where the kneading and solvent dilution time is less than 1 hour is indicated as “◯”, and “x” for 1 hour or more. Material ink processability was evaluated. Table 6 shows the results.

<Electrode characteristic evaluation of conductive composition for electrode>
Polyvinylidene fluoride PVDF (KF polymer W # 1100, manufactured by Kureha Co., Ltd.) and N-methyl-2-pyrrolidone as a binder are mixed with the conductive composition shown in Table 5 (6 parts as the amount of conductive material) with a high-speed disper. Then, 89 parts of lithium cobaltate LiCoO ₂ (HLC-17, average particle size 9.28 μm, specific surface area 0.54 m ² / g, manufactured by Honjo Chemical Co., Ltd.) as a positive electrode active material was added and kneaded by a planetary mixer. The mixture ink (solid content ratio: 60%, solid content composition ratio; active material / carbon black / binder and dispersant = 89/6/5) was used. Furthermore, after apply | coating using a doctor blade on the 20-micrometer-thick aluminum foil used as a collector, it heat-dried under reduced pressure, the rolling process by roll press etc. was performed, and the positive electrode of thickness 80 micrometers was produced. A load was applied to the produced positive electrode at 2 kgf / cm ² with an electric resistance measuring device A (manufactured by Imoto Seisakusho), and the electric conductivity in the thickness direction of the electrode was measured. This measurement was performed 5 times for each sample, and those whose average electric conductivity (10 ⁻³ S / cm) was 100 or more were evaluated as “「 ”, 10 (10 ⁻³ S / cm) or more, 100 (10 ^-3 what was S / cm) less ^{"○", 1 (10} -3 S / cm) or ^{more, 10 (10-3} what was S / cm) less than "△", 1 (10 ^- What was less than ³ S / cm) was defined as “x”. Usually, the electrical conductivity of lithium ion batteries and capacitors needs to be 10 ⁻³ S / cm or more. If the electric conductivity is lower than this value, it is presumed that the capacity and output characteristics are greatly affected and there is a defect as an electrode. The

The result of the electrode characteristic evaluation of the electroconductive composition for electrodes is shown in Table 6.
<Preparation of positive electrode mixture ink for lithium secondary battery>
[Examples 1-21, Comparative Examples 1-4]
Polyvinylidene fluoride PVDF (KF polymer W # 1100, Kureha Co., Ltd.) as a binder for the conductive compositions (1) to (21) and comparisons (1) to (5) of the present invention (5 parts as the amount of conductive material) And N-methyl-2-pyrrolidone mixed with a high-speed disper, and then used as a positive electrode active material lithium cobaltate LiCoO ₂ (HLC-17, average particle size 9.28 μm, specific surface area 0.54 m ² / g, Honjo Chemical 90 parts) was added and kneaded by a planetary mixer to obtain a positive electrode mixture ink (solid content ratio: 60%, solid content composition ratio; active material / carbon black / binder and dispersant = 90/5/5). . (See Table 8)

[Example 15, Comparative Example 6]
Polyvinylidene fluoride PVDF (KF polymer W # 1100, manufactured by Kureha Co.) and N-methyl-2-pyrrolidone as a binder were mixed with the conductive composition of the present invention (9 parts as the amount of carbon black) with a high-speed disper. Later, 85 parts of lithium manganate LiMn ₂ O ₄ (CELLSEED S-LM, average particle size 12 μm, specific surface area 0.48 m ² / g, manufactured by Nippon Chemical Industry Co., Ltd.) as a positive electrode active material was added and kneaded by a planetary mixer. Positive electrode mixture ink (solid content ratio: 60%, solid content composition ratio; active material / carbon black / binder and dispersant = 85/9/6) was used. (See Table 9)

[Example 18, Comparative Examples 8 and 9]
Lithium iron phosphate LiFePO ₄ (average particle size 3.6 μm, specific surface area 15 m ² / g, manufactured by TIAN JIN STL ENERGY TECHNOLOGY) 91 parts polyvinylidene fluoride PVDF (KF polymer W # 1100, Kureha) as binder Manufactured) and N-methyl-2-pyrrolidone after mixing with a planetary mixer, the conductive composition of the present invention (4 parts as carbon black) is added as a conductive aid, and further kneaded with a planetary mixer. A composite ink (solid content ratio: 50%, solid content composition ratio; active material / carbon black / binder and dispersant = 91/4/5) was used. (See Table 9)

[Examples 6 and 7, Comparative Example 4]
After mixing polytetrafluoroethane PTFE (PTFE 30-J, Mitsui / DuPont Fluoro Chemical Co., Ltd.) and water as a binder with a high-speed disper, the conductive composition of the present invention (carbon black amount 5 parts) As a positive electrode active material, 90 parts of lithium cobalt oxide LiCoO ₂ (HLC-17, average particle size 9.28 μm, specific surface area 0.54 m ² / g, manufactured by Honjo Chemical Co., Ltd.) was added and kneaded by a planetary mixer. (Solid content ratio: 60%, solid content composition ratio: active material / carbon black / binder and dispersant = 90/5/5). (See Table 8)

[Examples 16 and 17, Comparative Example 7]
Polytetrafluoroethane PTFE (PTFE 30-J, manufactured by Mitsui / Du Pont Fluoro Chemical Co.) as a binder and water with a high-speed disperser for the conductive composition of the present invention (9 parts as carbon black) prepared earlier. After mixing, 85 parts of lithium manganate LiMn ₂ O ₄ (CELLSEED S-LM, average particle size 12 μm, specific surface area 0.48 m ² / g, manufactured by Nippon Chemical Industry Co., Ltd.) was added as a positive electrode active material and kneaded by a planetary mixer. And positive electrode material ink (solid content ratio: 60%, solid content composition ratio; active material / carbon black / binder and dispersant = 85/9/6). (See Table 9)

[Examples 19 and 20, Comparative Example 9]
5 parts of polyvinylidene fluoride PVDF (KF polymer W # 1100, manufactured by Kureha) as a binder, N-methyl-2-pyrrolidone as a binder with respect to the conductive composition of the present invention (carbon black amount of 4 parts) prepared earlier. After mixing with a high speed disper, 91 parts of lithium iron phosphate LiFePO ₄ (average particle size 3.6 μm, specific surface area 15 m ² / g, manufactured by TIAN JIN STL ENERGY TECHNOLOGY) was added as a positive electrode active material and kneaded by a planetary mixer. And positive electrode mixture ink (solid content ratio: 60%, solid content composition ratio; active material / carbon black / binder and dispersant = 91/4/5). (See Table 9)

<Preparation of negative electrode ink for lithium secondary battery>
[Examples 21 and 30, Comparative Examples 10 and 13]
After mixing styrene butadiene rubber SBR (BM-400B, manufactured by Nippon Zeon Co., Ltd.) as a binder and water with a high-speed disper to the conductive composition of the present invention (2 parts as carbon black amount), mesophase as a negative electrode active material 93 parts of carbon (MCMB 6-28, average particle size 5 to 7 μm, specific surface area 4 m ² / g made by Osaka Gas Chemical Co., Ltd.) was added and kneaded with a planetary mixer, and negative electrode mixture ink (solid content ratio: 60%, solid Fractional composition ratio: active material / carbon black / binder and dispersant = 93/2/5). (See Table 10)

[Examples 21 to 29, 31, Comparative Examples 11, 12, and 14]
Polyvinylidene fluoride PVDF (KF polymer W # 1100, manufactured by Kureha) and N-methyl-2-pyrrolidone as a binder were mixed with the conductive composition of the present invention (2 parts as the amount of carbon black) with a high-speed disper. Later, 93 parts of mesophase carbon (MCMB 6-28, average particle size of 5 to 7 μm, specific surface area of 4 m ² / g manufactured by Osaka Gas Chemical Co., Ltd.) was added as a negative electrode active material and kneaded by a planetary mixer. 60%, solid composition ratio; active material / carbon black / binder and dispersant = 3/2/5). (See Table 10)

<Preparation of positive electrode for lithium secondary battery>
[Examples 1-20, Comparative Examples 1-9]
The various positive electrode mixture inks prepared above were applied onto a 20 μm thick aluminum foil serving as a current collector using a doctor blade, dried by heating under reduced pressure, and subjected to a rolling process using a roll press or the like to obtain a thickness of 60 μm. A positive electrode mixture layer was prepared. (See Tables 8 and 9)

<Assembly of lithium secondary battery positive electrode evaluation cell>
A separator made of a porous polypropylene film between the working electrode and the counter electrode (# 2400, manufactured by Celgard Co., Ltd.) with the positive electrode fabricated previously punched out to a diameter of 9 mm and used as a working electrode and a metal lithium foil (thickness 0.15 mm) as a counter electrode Are inserted and laminated, filled with an electrolyte (non-aqueous electrolyte in which LiPF ₆ is dissolved at a concentration of 1 M in a mixed solvent of ethylene carbonate and diethyl carbonate in a ratio of 1: 1), and a bipolar metal cell (Hosen) (HS flat cell). The cell was assembled in a glow box substituted with argon gas, and after the cell was assembled, predetermined battery characteristics were evaluated.

<Characteristic evaluation of lithium secondary battery positive electrode>
[Charge / Discharge Cycle Characteristics Examples 18 to 20, Comparative Examples 8 and 9]
The produced battery evaluation cell was fully charged at a constant current and constant voltage charge (upper limit voltage 4.2 V) at a room temperature (25 ° C.) with a charge rate of 0.2 C and 1.0 C, and at a constant current at the same rate as during charging. Charge / discharge for discharging to a discharge lower limit voltage of 3.0V is defined as one cycle (charge / discharge interval rest time 30 minutes), and this cycle is performed for a total of 20 cycles to evaluate charge / discharge cycle characteristics (Evaluation apparatus: SM-8 manufactured by Hokuto Denko Co., Ltd.) ) Moreover, the cell after evaluation was decomposed | disassembled and the external appearance of the electrode coating film was confirmed visually. The evaluation results are shown in Tables 11 and 12.

[Charge / Discharge Cycle Characteristics Examples 1-17, Comparative Examples 1-7]
The produced battery evaluation cell is fully charged at a constant current and constant voltage charge (upper limit voltage 4.5 V) at room temperature (25 ° C.) and at a charge rate of 0.2 C and 1.0 C, and at a constant current at the same rate as during charging. Charging / discharging for discharging to a lower discharge limit voltage of 2.0V is defined as one cycle (charging / discharging interval rest time 30 minutes), and this cycle is performed for a total of 20 cycles, and charging / discharging cycle characteristics evaluation (evaluation apparatus: SM-8 manufactured by Hokuto Denko Co., Ltd.) ) Moreover, the cell after evaluation was decomposed | disassembled and the external appearance of the electrode coating film was confirmed visually. The evaluation results are shown in Tables 11 and 12.

[DC Internal Resistance Measurement Examples 1 to 26, Comparative Examples 1 to 5]
The battery evaluation cell thus prepared was fully charged at a constant current and constant voltage charge (upper limit voltage 4.2 V) at room temperature (25 ° C.) and a charge rate of 0.2 C, and 5 at a constant current of 0.2 C and 1.0 C rates. The battery voltage was measured after the second discharge. The voltage value was plotted against the current value, and the slope of the obtained linear relationship was defined as the internal resistance. The evaluation results are shown in Tables 11 and 12. About the case where lithium cobaltate was used as a positive electrode active material, it showed as a relative value when the internal resistance measured value of Example 5 is set to 100. The cases where lithium manganate and lithium iron phosphate were used as the positive electrode active materials were shown as relative values when the measured values of internal resistance in Examples 15 and 19 were taken as 100.

<Preparation of negative electrode for lithium secondary battery>
[Examples 21 to 31, Comparative Examples 10 to 14]
The various negative electrode mixture inks prepared above were applied onto a copper foil having a thickness of 20 μm as a current collector using a doctor blade, then dried under reduced pressure, and subjected to a rolling process using a roll press or the like to obtain a thickness of 60 μm. A negative electrode mixture layer was prepared.

<Assembly of lithium secondary battery negative electrode evaluation cell>
A separator made of a porous polypropylene film between the working electrode and the counter electrode (# 2400, manufactured by Celgard Co., Ltd.) with the negative electrode prepared previously punched to a diameter of 9 mm and used as a working electrode, and a metallic lithium foil (thickness 0.15 mm) as a counter electrode Is inserted and laminated, filled with an electrolyte (nonaqueous electrolyte in which LiPF ₆ is dissolved at a concentration of 1M in a mixed solvent of ethylene carbonate and diethyl carbonate in a ratio of 1: 1), and a bipolar metal cell (Hosen) (HS flat cell). The cell was assembled in a glove box substituted with argon gas, and after the cell was assembled, the following battery characteristics were evaluated.

<Characteristic evaluation of lithium secondary battery negative electrode>
[Charge / Discharge Cycle Characteristics Example 21-31, Comparative Example 10-14]
The battery evaluation cell thus prepared was fully charged at 0.05 V by constant current and constant voltage charging at room temperature (25 ° C.), charging rate of 0.2 C and 1.0 C, and the voltage was constant at the same rate as charging. Charging / discharging for discharging until 1.5V was taken as one cycle (charging / discharging interval rest time 30 minutes).
First, this charge / discharge operation was performed five times, and the discharge capacity at the sixth time was set as an initial value. Then, this cycle was performed 20 times in total, and charge / discharge cycle characteristic evaluation (evaluation apparatus: SM-8 manufactured by Hokuto Denko) was performed. Moreover, the cell after evaluation was decomposed | disassembled, the presence or absence of the electrode coating film defect was confirmed visually, and the thing without a problem was set as "(circle)". The evaluation results are shown in Table 10 and Table 13.

<Capacitor electrode characteristic evaluation of conductive composition for electrode>
Polyvinylidene fluoride PVDF (KF polymer W # 1100, manufactured by Kureha Co., Ltd.) and N-methyl-2-pyrrolidone as a binder are mixed with the conductive composition shown in Table 5 (5 parts of conductive material) as a binder. Thereafter, 79 parts of activated carbon powder (“Fine activated carbon RP20” manufactured by Kuraray Chemical Co., Ltd.) as a positive electrode active material: average particle size 5.0 μm, specific surface area 2000 m ² / g) was added and kneaded with a planetary mixer, and a composite ink for capacitors (Solid content ratio: 60%, solid content composition ratio: active material / carbon black / binder and dispersant = 79/5/16). Furthermore, after apply | coating using a doctor blade on the 20-micrometer-thick aluminum foil used as a collector, it heat-dried under reduced pressure, the rolling process by roll press etc. was performed, and the 90-micrometer-thick capacitor electrode was produced. A load was applied to the prepared electrode at 2 kgf / cm ² with an electric resistance measuring device A (manufactured by Imoto Seisakusho), and the electric conductivity in the thickness direction of the electrode was measured. This measurement was performed 5 times for each sample, and those whose average electric conductivity (10 ⁻³ S / cm) was 100 or more were evaluated as “「 ”, 10 (10 ⁻³ S / cm) or more, 100 (10 ^-3 what was S / cm) less ^{"○", 1 (10} -3 S / cm) or ^{more, 10 (10-3} what was S / cm) less than "△", 1 (10 ^- What was less than ³ S / cm) was defined as “x”. Usually, the electrical conductivity of lithium ion batteries and capacitors needs to be 10 ⁻³ S / cm or more. If the electric conductivity is lower than this value, it is presumed that the capacity and output characteristics are greatly affected and there is a defect as an electrode. The

As a result of the above, all of the electrode conductive compositions (1) to (21) had an electric conductivity of 10 ⁻¹ S / cm or more and an evaluation of “◎”. Moreover, evaluation was also "(circle)" also about handling property and compound-material ink processability. On the other hand, the comparative compositions (1) to (5) had an electrical conductivity of “Δ”, but the handling properties and composite ink processability were also “x”. Therefore, the conductive composition for electrodes of the present invention can also be suitably used for capacitors.

Claims (12)

A conductive composition comprising a conductive material, a solvent, and a wetting improver,
The conductive material has a bulk density of 0.01 to 0.20 g / cm ³ and a volume resistivity of 0.001 to 0.1 Ω · cm (when the compression density is 0.9 g / cm ³ ).
The conductive composition for electrodes, wherein the conductive composition is granular and has a solid content of 20 to 60% by weight. The wettability improver is a compound having two or more polar functional groups per molecular unit, and the conductive composition is granular and has a solid content of 25 to 55% by weight. Item 2. The conductive composition for an electrode according to Item 1. The wettability improver is a compound having two or more polar functional groups per molecular unit, and the wettability improver has a molecular weight of 50 to 1000 or less and a weight average molecular weight of 3000 to 2 million or less. 3. The conductive composition for an electrode according to claim 1 or 2, comprising a wetting improver B. The electrode conductive material according to any one of claims 1 to 3, wherein the conductive material is at least one selected from the group consisting of acetylene black, furnace black, ketjen black, graphite, graphitized carbon, and fibrous carbon material. Composition. The conductive composition for electrodes according to any one of claims 1 to 4, wherein the granular conductive composition has a bulk density of 0.30 to 0.80 g / cm ³ . The conductive composition for an electrode according to any one of claims 1 to 5, wherein the conductive composition is medialessly dispersed. The conductive composition for electrodes according to any one of claims 1 to 6, wherein the conductive composition is subjected to high-speed shear dispersion with a stirring blade and / or a stirring blade. The conductive material for an electrode according to any one of claims 1 to 7, wherein the conductive material is subjected to a first step of wetting the conductive material with a solvent with a wetting improver and a second step of granulating the wetted conductive material. Method for producing a composition.   The electroconductive composition for electrodes formed using the manufacturing method of Claim 8.   The electrode for positive electrodes or negative electrodes formed using the electroconductive composition for electrodes in any one of Claims 1-7, 9.   The secondary battery formed using the electrode for positive electrodes or negative electrodes of Claim 10. The capacitor formed using the electrode for positive electrodes or negative electrodes of Claim 10.