JP5663237B2 - Carbon material composite particles and method for producing the same - Google Patents

Description

  The present invention relates to a carbon material composite particle in which a carbon material is composited on the surface of a polymer particle and a method for producing the same.

  Conventionally, carbon nanotube composite particles in which carbon nanotubes are combined on the particle surface have been developed. These composite particles have many application examples. For example, they have been formed into a composite and solidified (Patent Document 1) or applied as a negative electrode active material for a lithium ion battery. As a method for producing carbon nanotube composite particles, a method of fixing or combining carbon nanotubes on the particle surface by applying compressive force and shear force in a state where one or more kinds of powder particles and carbon nanotubes are mixed has been proposed. (Patent Document 2).

International Publication WO 2009/054309 JP-A-2005-014201

  Even in the method for producing the composite particles, since the carbon material itself is cohesive, the carbon material is agglomerated during mixing, and the amount of the carbon material adhering to the composite particles obtained varies. Occurred and the uniformity was insufficient. Accordingly, an object of the present invention is to provide a composite polymer particle in which a carbon material is composited more uniformly in a method for producing a carbon material composite particle in which a carbon material is adhered to the particle surface, and a method for producing the composite polymer particle. And

The present invention (1) includes a cylindrical casing that stores an object to be fluidized, and stirring means installed in a lower portion of the casing, and the stirring means is stored in the casing by rotating. Using an agitating device having at least an ascending agitating blade for generating an ascending flow in an object and a shearing agitating blade for shearing an object housed in the casing by rotating,
A mixing step in which a dispersion containing a carbon material and a solvent, and polymer particles are introduced into a casing of the stirring device and stirred by the stirring means to prepare a paste-like material;
A stirring and drying step of evaporating and drying the solvent while stirring the prepared paste-like material;
It is a manufacturing method of the carbon material composite grain | particle characterized by having.

  The present invention (2) is the production method of the invention (1), wherein the carbon material is a carbon nanotube.

  The present invention (3) is characterized in that, in the stirring and drying step, the solvent is evaporated by frictional heat generated by rotating an upflow stirring blade and a shear stirring blade of the stirring means. ) Or (2).

  The present invention (4) is the manufacturing method according to any one of the inventions (1) to (3), characterized in that in the stirring and drying step, heating is performed from the outside.

  The present invention (5) is the manufacturing method according to any one of the inventions (1) to (4), wherein the inside of the casing is depressurized in the stirring and drying step.

  The present invention (6) is characterized in that, in the mixing step, the dispersion is mixed with the particles while the particles are flowed by the stirring means. One of the manufacturing methods.

  The present invention (7) is the production method of any one of the inventions (1) to (6), wherein a solvent is further introduced in the mixing step.

  The present invention (8) is the production method according to any one of the inventions (1) to (7), characterized in that, in the mixing step, the viscosity of the paste-like material is 100 Pa · s or less. is there.

The present invention (9) has polymer particles and a carbon material compounded on the surface of the polymer particles,
The carbon material composite particles are characterized in that the standard deviation / carbon amount average value is 0.1 or less as a result of measuring the carbon content (wt%) in the carbon material composite particles.

In the present invention (10), the carbon material composite particles are:
A housing for storing an object to be flowed; and stirring means installed at a lower portion of the housing, the stirring means for generating an upward flow in the object stored in the housing by rotating the stirring means. Using an agitator having at least an upflow agitating blade and a shear agitating blade for shearing an object housed in the casing by rotating,
A dispersion containing a carbon material and a solvent, and polymer particles are introduced into the casing of the stirring device, and are stirred by the stirring means to prepare a paste-like material, while stirring the paste-like material, The carbon material composite particles according to the invention (9), which are obtained by evaporating a solvent and drying.

  The present invention (11) is the carbon material composite particle according to the invention (9) or (10), wherein the carbon material is a carbon nanotube.

  Here, various terms used in this specification will be described. “Carbon material composite particles” include particles whose surfaces are coated with carbon materials (for example, carbon nanotubes), particles whose carbon materials are attached to the surfaces, and carbon materials whose surfaces are coated with particles. In addition, it means a particulate material in which a carbon material and particles are included in the configuration.

  According to the present invention, the carbon material and the polymer particles are mixed with the polymer particles by preparing a paste by mixing the carbon material that is easily aggregated by using the carbon material dispersion, and mixing with the polymer particles. Mix evenly. Furthermore, carbon material composite particles in which polymer particles and carbon material are uniformly combined can be obtained by evaporating and drying the solvent while stirring. Moreover, when the stirring layer apparatus to be used has an upflow stirring blade and a shear stirring blade, the combination of these stirring blades makes it possible to obtain polymer particles in which the carbon material is more uniformly combined.

FIG. 1 is a schematic configuration diagram of a stirring device used in the production method according to the present invention. FIG. 2 is a schematic configuration diagram illustrating an example of an upflow stirring blade. FIG. 3 is a schematic configuration diagram illustrating an example of a shear stirring blade.

  Hereinafter, the apparatus and materials used in the manufacturing method according to the present invention will be described, and each process will be described in detail.

  First, the stirring device used in the production method according to the present invention will be described. FIG. 1 is a schematic configuration diagram of a stirring device used in the production method according to the present invention. The stirring device 100 includes a cylindrical casing 110 that stores an object to be fluidized, and stirring means 120 installed at a lower portion in the casing. The case 110 includes a heating unit 111 that heats the periphery of the case. The heating means may be a jacket in which a heating fluid such as steam flows or a heater that electrically heats the housing. The outside of the heating means may be covered with a heat insulating material 112.

  The stirring device according to the present invention preferably has a decompression means 130 for arranging the inside of the housing under a reduced pressure. Although it does not specifically limit as a pressure reduction means, For example, a vacuum pump is mentioned. The decompression unit is connected to the housing 110 via the pipe 131.

  The agitating means used in the present invention is housed in the casing by rotating with an upflow agitating blade (lower blade) 123 for generating an upward flow in the object housed in the casing by rotating. And at least a shear stirring blade (upper blade) 121 for shearing the object. Although the case where two blades constituting the stirring unit are used as an example is shown, the present invention is not limited to this and may have three or more blades.

  The upflow stirring blade 123 and the shear stirring blade 121 are connected to a rotating shaft 125, and the shaft 125 is connected to a rotating means 127 such as a motor, and the blade rotates by rotating the rotating means. Then, the object M arranged in the housing is agitated.

  The shape of the upflow agitating blade is not particularly limited. For example, it has a rotating shaft center portion that fits the rotating shaft and a blade portion that extends from the rotating shaft center portion, and the end of the blade portion curves upward. Has a structured. Since the end of the blade portion is curved upward, an upward flow is generated in the casing, and the object is rotated in the casing. Moreover, it is preferable that an upflow stirring blade is installed in the bottom face of a housing | casing. By being installed on the bottom surface in this way, the object accumulated in the lower part of the casing is scraped up and an upward flow is generated, so that the carbon material and the particles are more uniformly combined.

  FIG. 2 is a schematic configuration diagram illustrating an example of an upflow stirring blade. In addition, an upflow stirring blade is not limited to this aspect, It shows as a specific example. The upflow agitating blade 1230 has a rotating shaft connecting portion 1231 that can be connected to the rotating shaft 125 and two stirring blades 1233 provided around the rotating shaft connecting portion. An edge portion 1235 for generating an upward flow is formed on one side of the stirring blade 1233. Moreover, it is suitable for the terminal of the stirring blade to have a curved portion 1237 that is curved upward.

  The shape of the shear stirring blade is not particularly limited as long as a shearing force with a flowing object such as a paste can be applied by stirring inside the casing. The shear stirring blade is preferably installed on the upper part of the upflow stirring blade. When the upward flow generated by the upward flow stirring blades reaches the upper portion of the object M by changing the flow direction to the bottom, the flow is changed to the bottom again. By arranging the shear stirring blade at the position where the flow is changed to the bottom in this way, the object is sheared more uniformly and mixed uniformly.

  FIG. 3 is a schematic configuration diagram of a shear stirring blade. In addition, although a shear stirring blade is not limited to this aspect, it shows as a specific example. The shear stirring blade 1210 includes a rotating shaft connecting portion 1211 that can be connected to the rotating shaft 125, a ring-shaped support 1213, a plurality of joint supports 1215 for connecting the ring-shaped support and the rotating shaft connecting portion, And a blade 1217 provided on the outer periphery of the annular support. A wake plate 1219 may be provided at the rear of the blade 1217 in the rotational direction. Here, an embodiment in which four blades are provided is shown, but the number is not limited to this number. For example, two or six blades may be used. In addition, it is preferable that the ring-shaped support body 1213 is configured to be disposed above the rotation shaft connecting portion 1211. Such an arrangement facilitates shearing.

  By introducing the object M to be flowed into the stirring device and stirring by the stirring means, the upward flow U is generated by the rotation of the upward flow stirring blade, and the entire body can be flowed and mixed in the mixer. . Furthermore, since the shearing force can be applied to the flowing object M by rotating the stirring means, the object is suitably mixed by the shearing force. In this way, by combining the upward flow and the shearing action, the particles and the carbon material dispersion are suitably mixed, so that the obtained carbon material composite particles are particularly remarkably uniform.

Polymer Particles The average particle diameter of the polymer particles used in the present invention is not particularly limited, but for example, about 0.1 μm to 10 mm is preferable.

  Examples of the polymer include polyolefin resins such as polyethylene and polypropylene, polyethylene terephthalate (PET), polytrimethylene terephthalate (PTT), polybutylene terephthalate (PBT), polyethylene naphthalate (PEN), polybutylene naphthalate (PBN), and the like. Polyester resins, nylon resins such as nylon 11, nylon 12, nylon 6 and nylon 66, polyimide resins, urethane resins, natural rubber, styrene / butadiene rubber, chloroprene rubber, butyl rubber and other rubber materials, acrylonitrile / Acrylic resins such as butadiene / styrene resin (ABS resin), polyacrylic acid, polyalkyl acrylate, polytetrafluoroethylene (PTFE), polychlorotrifluoroethylene (PC) FE), polyvinylidene fluoride (PVDF), polyvinyl fluoride (PVF), perfluoroalkoxy fluororesin (PFA), ethylene tetrafluoride / hexafluoropropylene copolymer (FEP), ethylene / tetrafluoroethylene copolymer (ETFE), fluororesin such as ethylene / chlorotrifluoroethylene copolymer (ECTFE).

Dispersion The dispersion used in the present invention contains a carbon material and a solvent. It is preferred that a dispersant is optionally contained.

  The carbon material in the present invention means an inorganic carbon material, and more specifically, carbon black, graphite, carbon fiber, nanocarbon and the like can be mentioned. Among these carbon materials, nanocarbon is preferable, and among the nanocarbons, carbon nanotubes are preferable. “Nanocarbon” as used herein means a carbon material having a diameter of 1000 nm or less. For example, carbon nanotubes (single-layer / double-layer / multi-layer type, cup-stack type), carbon nanofiber, carbon nanohorn or fullerene are used. Can be mentioned. The carbon nanotube may be a single wall carbon nanotube (SWCNT) or a multi-wall carbon nanotube (MWCNT). The length of the carbon nanotube is preferably from 0.1 to 100 μm, more preferably from 0.1 to 50 μm, and further preferably from 0.1 to 20 μm. The diameter of the carbon nanotube is preferably 5 to 200 nm, more preferably 8 to 160 nm, and still more preferably 9 to 120 nm. In addition, the length and diameter of the tube are measured with respect to 100 or more structures existing within a predetermined range using an AFM (atomic force microscope), and set to a range in which 90% or more are included.

  Also, the carbon nanotube synthesis method is not particularly limited, and any synthesis method such as an electric discharge method (C. Journet et al., Nature 388, 756 (1997) and DS Bethune et al., Nature 363, 605 (1993) )), Laser deposition (RESmally et al., Science 273, 483 (1996)), gas phase synthesis (R. Andrews et al., Chem. Phys. Lett., 303,468, 1999), thermochemical vapor phase Vapor deposition (WZLi et al., Science, 274, 1701 (1996), Shinohara et al., Jpn. J. Appl. Phys. 37, 1257 (1998)), plasma enhanced chemical vapor deposition (ZFRen et al. , Science. 282, 1105 (1998)) or the like. In addition, about the crude product in which the metal catalyst was used in the synthesis | combination, it is suitable to process with an acid and to remove a metal catalyst. Regarding acid treatment, for example, as disclosed in JP-A-2001-26410, a nitric acid solution or a hydrochloric acid solution is used as an aqueous acid solution. For example, a nitric acid solution is diluted 50 times with water, and a hydrochloric acid solution is also 50 times. A method using a solution diluted in water can be mentioned. And after acid-treating in this way, it wash | cleans and filters and it is set as carbon nanotube aqueous solution.

The dispersant is not particularly limited. For example, phospholipid surfactants, amphoteric surfactants, nonionic surfactants, anionic surfactants, cationic surfactants and other surfactants, Examples include host compounds that form inclusion compounds such as dextrins, and other naturally-occurring polymer compounds such as nucleic acids and proteins. “Phospholipid surfactants” are anionic and zwitterionic surfactants that have phosphate groups as functional groups, including phospholipids (including both glycerophospholipids and sphingophospholipids) Any of phospholipids (for example, hydrogenated phospholipids, lysophospholipids, enzyme-converted phospholipids, lysophosphatidylglycerol, and complexes with other substances) may be used. Such phospholipids are present in various membrane systems of the cells that make up organisms, such as the plasma membrane, nuclear membrane, endoplasmic reticulum membrane, mitochondrial membrane, Golgi membrane, lysosomal membrane, chloroplast membrane, and bacterial cell membrane. Preferably, phospholipids used for preparing liposomes are suitable. Specifically, for example, phosphatidylcholine {for example, distearoylphosphatidylcholine (DSPC), dimyristoylphosphatidylcholine (DMPC), dipalmitrylphosphatidylcholine (DPPC)}, phosphatidylethanolamine, phosphatidylinositol, phosphatidylserine, phosphatidylglycerol, diphosphatidylglycerol Lysophosphatidylcholine and sphingomyelin. Particularly preferred surfactants are zwitterionic surfactants. Zwitterionic surfactants include quaternary ammonium base / sulfonic acid group (—SO ₃ H) type, quaternary ammonium base / phosphate group (soluble in water), quaternary ammonium base / phosphate group. Examples include amphoteric surfactants of the type (insoluble in water) and quaternary ammonium base / carboxyl group type. The acid group may be a salt. In particular, the zwitterionic surfactant preferably has both + and-charges in one molecule, and the acid dissociation constant (pKa) of the acid group is preferably 5 or less. More preferably, it is more preferably 3 or less. Specifically, 3-[(3-colamidopropyl) dimethylamino] -2-hydroxy-1-propanesulfonic acid (CHAPSO), 3-[(3-colamidopropyl) dimethylamino] -propanesulfonic acid ( CHAPS), N, N-bis (3-D-gluconamidopropyl) -colamide, n-octadecyl-N, N′-dimethyl-3-amino-1-propanesulfonic acid, n-decyl-N, N ′ -Dimethyl-3-amino-1-propanesulfonic acid, n-dodecyl-N, N'-dimethyl-3-amino-1-propanesulfonic acid, n-tetradecyl-N, N'-dimethyl-3-amino-1 -Propanesulfonic acid {Zwittergent (TM) -3-14}, n-hexadecyl-N, N'-dimethyl-3-amino-1-propanesulfonic acid, n-octadecyl-N Ammonium sulfobetaines such as N'-dimethyl-3-amino-1-propanesulfonic acid, n-octylphosphocholine, n-nonylphosphocholine, n-decylphosphocholine, n-dodecylphosphocholine, n-tetradecylphosphocholine Phosphocholines such as choline and n-hexadecylphosphocholine, phosphatidylcholines such as dilauroylphosphatidylcholine, dimyristoylphosphatidylcholine, dipalmitoylphosphatidylcholine, distearoylphosphatidylcholine, dioleoylphosphatidylcholine, and dilinoleoylphosphatidylcholine. The solvent is not particularly limited, but water is particularly preferable because of easy handling and dispersion.

  In the present invention, the solvent is not particularly limited, and examples thereof include an aqueous solvent and an organic solvent.

  The aqueous solvent used in the present invention is water or water and a hydrophilic solvent (for example, alcohols such as methanol and ethanol, ketones such as acetone and 2-butanone (MEK), dimethylformamide (DMF), and N-methyl. And amides such as pyrrolidone (NMP) and ethers such as tetrahydrofuran (THF)).

  The organic solvent is not particularly limited. For example, aromatic hydrocarbons such as toluene, benzene, xylene, styrene, ethylbenzene, chloroaromatic hydrocarbons such as chlorobenzene, ortho-dichlorobenzene, and chlorinated aliphatic hydrocarbons. Methylene chloride, chloroform (trichloromethane), carbon tetrachloride (tetrachloromethane), 1,2-dichloroethane, 1,1,1-trichloroethane, 1,1,2,2-tetrachloroethane, 1, 2-dichloroethylene, trichloroethylene, trachlorethylene (perchlorethylene), alcohols such as methanol (methyl alcohol), isopropyl alcohol, 1-butanol, 2-butanol, isobutyl alcohol, isopentyl alcohol (isoamyl alcohol), Butyl alcohol, Clohexanol, esters such as methyl acetate, ethyl acetate, propyl acetate, isopropyl acetate, butyl acetate, isobutyl acetate, pentyl acetate (amyl acetate), isopentyl acetate (isoamyl acetate), ethyl ethers such as 1,4- Dioxane, tetrahydrofuran, dioxane, ketones such as acetone, methyl ethyl ketone, methyl butyl ketone, methyl isobutyl ketone, cyclohexanone, isophone, glycol ethers (cellosolve) such as ethylene glycol monomethyl ether (methyl cellosolve), ethylene glycol monoethyl ether (cellosolve) ), Ethylene glycol monobutyl ether (butyl cellosolve), ethylene glycol monoethyl ether acetate (cellosolve acetate), fat Hydrocarbons and their derivatives cyclohexane, cyclohexanone, methylcyclohexanone, cyclohexanol, methylcyclohexanol, aliphatic hydrocarbons normal hexane, mixtures of aliphatic or aromatic hydrocarbons, gasoline, benzine, rubber volatilization Oil, soybean volatile oil, mineral spirit, cleaning solvent, coal tar naphtha (boiling range 120-160 ° C, 120-180 ° C, 140-200 ° C), petroleum ether, petroleum naphtha, petroleum benzine, mineral spirit, alicyclic carbonization Hydrogen (turpentine oil), mixed hydrocarbons (HAWS, sorbet 100, sorbet 150), glycols (ethylene glycol, propylene glycol, diethylene glycol, polyethylene glycol, polypropylene glycol) , Diethylene glycol monoethyl ether, polypropylene glycol monoethyl ether, polyethylene glycol monoallyl ether, polypropylene glycol monoallyl ether, ethyl cellosolve, butyl cellosolve, carbitol, butyl carbitol, methoxybutanol) and ester ethers (cellosolve acetate, butyl cellosolve acetate, acetic acid) Carbitol, methoxybutyl acetate), silicone oils (polydimethylsiloxane, partially octyl-substituted polydimethylsiloxane, partially phenyl-substituted polydimethylsiloxane), halogenated hydrocarbons (chlorobenzene, dichlorobenzene, chloroform, bromobenzene, dichloromethane, trichloromethane) , Fluorides, other cresols, carbon disulfide, N, N Dimethylformamide and the like. Two or more of these may be mixed. Among these solvents, methyl ethyl ketone and toluene are preferred from the viewpoint of dispersibility and ease of removal / recovery.

  The concentration of the carbon material contained in the dispersion according to the present invention is preferably 0.2 to 50 wt%, more preferably 0.5 to 20 wt%, and further preferably 1 to 10 wt%. . Moreover, 0.01-100 are suitable for the weight ratio with respect to the carbon material of a dispersing agent, 0.05-20 are more suitable, and 0.1-10 are still more suitable.

  The production method according to the present invention will be described by taking an example using the above stirring device. The production method according to the present invention includes a mixing step of preparing a paste-like material by mixing a carbon material dispersion and polymer particles using a stirring device, and evaporating the solvent while stirring the paste-like material. This is a method for producing carbon material composite particles through a drying and drying step. Moreover, you may have the process of adding additives other than a carbon material arbitrarily.

In the mixing step, the paste material is prepared by mixing the carbon material dispersion and the polymer particles using the agitator described above. By using a carbon material dispersion in the process, the case of carbon nanotubes will be described as an example. Compared to the case of using powdered carbon nanotubes, the carbon nanotubes are less aggregated, and further in the mixing process. Once the paste is made into a paste, it can be placed under conditions that make it difficult for the carbon nanotubes to aggregate. As a result, it is possible to obtain particles in which the carbon nanotubes are uniformly complexed.

  Here, when the carbon material dispersion and the polymer particles are mixed, the polymer particles are first put in the casing of the stirring device and stirred by the stirring means. By slowly putting the carbon material dispersion into the casing while stirring the particles, the powder is less likely to become lumpy and a uniform paste can be obtained. In addition, when the carbon material dispersion liquid is not added and the fluidity is not sufficient, a solvent may be further added to impart fluidity to the paste.

  Here, the viscosity of the paste-like material prepared in the mixing step is preferably 100 Pa · s or less, more preferably 50 Pa · s or less, and further preferably 10 Pa · s or less. It is. The lower limit is not limited, and may be a liquid that is difficult to measure viscosity, but is, for example, 0.01 Pa · s. However, if the solvent is added until it becomes liquid, it takes a lot of time and energy to evaporate the solvent in the drying step described later, which is not preferable from the viewpoint of work efficiency.

Stirring and drying step In the stirring and drying step, the solvent contained in the pasty material is evaporated and dried while stirring the pasty material prepared in the mixing step. By having the stirring and drying step in this manner, the carbon material and the polymer particles can be uniformly combined by volatilizing the solvent while stirring. At this time, it is also possible to volatilize the solvent by frictional heat generated by rotating the stirring blade of the stirring device at a high speed. By volatilizing in this way, the energy used in the production can be minimized, and the solvent evaporates while receiving shearing force due to the rotation of the blades, making it difficult for the carbon material to coagulate. Uniform composite particles can be obtained. In the stirring and drying step, for example, heating may be performed from the outside by a heating unit of a stirring device or the like. It is preferable because the solvent can be evaporated more rapidly by heating.

  In this step, it is preferable to reduce the pressure in the housing. The decompression can be performed by, for example, decompression means of a stirring device. In this way, since the boiling point of the solvent is lowered by reducing the pressure, the temperature of the mixture can be kept low, so even if the particles are heat-sensitive materials, the properties of the particles are hardly changed. Can be processed.

  When the solvent evaporates from the paste-like material in this step, carbon material composite particles can be obtained. Since the carbon material composite particles obtained here are manufactured by the manufacturing method, the carbon material is uniformly composited with the particles. The composite particles obtained in the present invention preferably have a mode in which polymer particles are coated with a carbon material.

  The polymer particles according to the present invention measure the amount of carbon (wt%) derived from carbon nanotubes using a thermal analysis (TG) method. The calculation and preferred range of the numerical value (standard deviation / carbon amount average value) are the same as described above.

  The carbon material composite particles obtained by the production method according to the present invention are used for reinforcing materials, conductive materials and the like as various molded articles after being processed by extrusion and pressing through a process such as kneading, for example. be able to.

Example 1
2400 g of polytetrafluoroethylene (PTFE), carbon nanotubes (CNT: VGCF-S, 10 wt% manufactured by Showa Denko) and 3- (N, N-dimethyltetradecylammonio) propane sulfonate (dispersant manufactured by Fluka) 960 g of a dispersion containing 44 wt% and 2081 g of water were put into a Henschel mixer FM20BX (manufactured by Nihon Coke Industries) equipped with a cylindrical casing and upflow stirring blades and shear stirring blades provided therein. , And stirred at 600 rpm for 30 seconds. The viscosity of the paste at that time was 8.3 Pa · s (measuring instrument: TVC-5 type viscometer manufactured by Toki Sangyo Co., Ltd., rotor: No. 4, rotation speed 20 rpm, measurement temperature: normal temperature 25 ° C.). Steam was introduced into a jacket covering the housing surface and heated, and at the same time, the pressure was reduced to 60 mmHg. Further, the water was removed by evaporation while stirring, and then PTFE combined with CNT was taken out. Using the thermal analysis (TG) method (measured by SII Nanotechnology Inc., EXSTAR TG / DTA7200), the amount of carbon derived from the carbon nanotubes of the carbon nanotube composite material three times while changing the sampling location in the same sample (Wt%) was measured (Table 2).

(Comparative Example 1)
It carried out similarly to the Example using the normal screw-shaped stirring blade, without using a Henschel mixer. The mixture was dried by heating to obtain a PTFE composite.

(Uniformity evaluation test)
In the uniformity evaluation test, determination was made based on the number of aggregates of 5 mm or more in 500 g of the sample. The case where the number of aggregates was 0 was evaluated as ○, the case where it was less than 5 as Δ, and the case where it was 5 or more as ×.

  The carbon material composite polymer particles according to the present invention can be applied to polymer composites and the like.

DESCRIPTION OF SYMBOLS 100: Agitation apparatus 110: Housing | casing 111: Heating means Heating means 112: Insulation material 120: Agitation means 121: Shear stirring blade 123: Upflow stirring blade 125: Rotating shaft 127: Rotating means 130: Decompression means 131: Piping 1210: Shear stirring blade 1211: Rotating shaft connecting portion 1213: Ring-shaped support 1215: Bonding support 1217: Blade 1219: Current plate 1230: Upflow stirring blade 1231: Rotating shaft connecting portion 1233: Stirring blade 1235: Edge portion 1237: Curve Part M: Object U: Upflow

Claims (8)

It has a cylindrical casing for storing the object to be flowed and a stirring means installed at the lower part of the casing, and the stirring means generates an upward flow in the object stored in the casing by rotating. Using an agitating device having at least an upflow agitating blade for rotating and a shear agitating blade for shearing an object housed in the casing by rotating,
A mixing step in which a dispersion containing a carbon material and a solvent, and polymer particles are introduced into a casing of the stirring device and stirred by the stirring means to prepare a paste-like material;
A stirring and drying step of evaporating and drying the solvent while stirring the prepared paste-like material;
A method for producing carbon material composite particles, comprising:   The manufacturing method according to claim 1, wherein the carbon material is a carbon nanotube.   The method according to claim 1 or 2, wherein, in the stirring and drying step, the solvent is evaporated by frictional heat generated by rotating an upflow stirring blade and a shear stirring blade of the stirring means.   The manufacturing method according to any one of claims 1 to 3, wherein in the stirring and drying step, heating is performed from the outside.   The manufacturing method according to claim 1, wherein the inside of the housing is depressurized in the stirring and drying step.   The manufacturing method according to claim 1, wherein in the mixing step, the dispersion is mixed with the particles while the particles are flowed by the stirring means.   In the said mixing process, a solvent is introduce | transduced further, The manufacturing method as described in any one of Claims 1-6 characterized by the above-mentioned.   In the said mixing process, the viscosity of the said paste-form thing is made into the viscosity of 100 Pa.s or less, The manufacturing method as described in any one of Claims 1-7 characterized by the above-mentioned.

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