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WO2011077598A1 - Carbon-fiber composite material, process for producing same, insulation article, electronic component, and logging tool - Google Patents

Carbon-fiber composite material, process for producing same, insulation article, electronic component, and logging tool Download PDF

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Publication number
WO2011077598A1
WO2011077598A1 PCT/JP2009/071907 JP2009071907W WO2011077598A1 WO 2011077598 A1 WO2011077598 A1 WO 2011077598A1 JP 2009071907 W JP2009071907 W JP 2009071907W WO 2011077598 A1 WO2011077598 A1 WO 2011077598A1
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WO
WIPO (PCT)
Prior art keywords
carbon
composite material
fiber composite
carbon nanofiber
carbon fiber
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/JP2009/071907
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French (fr)
Japanese (ja)
Inventor
徹 野口
宏之 植木
茂樹 犬飼
悟史 飯生
正栄 伊藤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Schlumberger Canada Ltd
Services Petroliers Schlumberger SA
MEFS KK
Hitachi Astemo Ltd
Schlumberger Technology BV
Schlumberger Holdings Ltd
Prad Research and Development Ltd
Original Assignee
Schlumberger Canada Ltd
Services Petroliers Schlumberger SA
Nissin Kogyo Co Ltd
MEFS KK
Schlumberger Technology BV
Schlumberger Holdings Ltd
Prad Research and Development Ltd
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Filing date
Publication date
Application filed by Schlumberger Canada Ltd, Services Petroliers Schlumberger SA, Nissin Kogyo Co Ltd, MEFS KK, Schlumberger Technology BV, Schlumberger Holdings Ltd, Prad Research and Development Ltd filed Critical Schlumberger Canada Ltd
Priority to JP2011547231A priority Critical patent/JP5647152B2/en
Priority to PCT/JP2009/071907 priority patent/WO2011077598A1/en
Publication of WO2011077598A1 publication Critical patent/WO2011077598A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/005Reinforced macromolecular compounds with nanosized materials, e.g. nanoparticles, nanofibres, nanotubes, nanowires, nanorods or nanolayered materials
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B82NANOTECHNOLOGY
    • B82YSPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
    • B82Y30/00Nanotechnology for materials or surface science, e.g. nanocomposites
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D10/00Physical treatment of artificial filaments or the like during manufacture, i.e. during a continuous production process before the filaments have been collected
    • D01D10/02Heat treatment
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F11/00Chemical after-treatment of artificial filaments or the like during manufacture
    • D01F11/10Chemical after-treatment of artificial filaments or the like during manufacture of carbon
    • D01F11/12Chemical after-treatment of artificial filaments or the like during manufacture of carbon with inorganic substances ; Intercalation
    • D01F11/122Oxygen, oxygen-generating compounds
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01BCABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
    • H01B3/00Insulators or insulating bodies characterised by the insulating materials; Selection of materials for their insulating or dielectric properties
    • H01B3/002Inhomogeneous material in general
    • H01B3/004Inhomogeneous material in general with conductive additives or conductive layers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2321/00Characterised by the use of unspecified rubbers
    • EFIXED CONSTRUCTIONS
    • E21EARTH OR ROCK DRILLING; MINING
    • E21BEARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B47/00Survey of boreholes or wells
    • E21B47/01Devices for supporting measuring instruments on drill bits, pipes, rods or wirelines; Protecting measuring instruments in boreholes against heat, shock, pressure or the like

Definitions

  • the present invention relates to a carbon fiber composite material and a manufacturing method thereof, an insulating article, an electronic component, and a logging apparatus.
  • Carbon nanofibers are excellent in mechanical properties and are expected to be applied in various fields as composite materials.
  • carbon nanofibers are also excellent in electrical conductivity, it has been proposed that a carbon fiber composite material in which carbon nanofibers are uniformly dispersed in an elastomer is applied to, for example, an electron emission device (for example, JP 2008-311083).
  • composite materials in which carbon nanofibers are blended with elastomers are excellent in mechanical properties, and thus are expected to be used in various applications as substitutes for conventional rubber products.
  • many of these conventional rubber products use the insulating properties of rubber, but carbon fiber composites with uniformly dispersed carbon nanofibers can conduct electricity even with a small amount of carbon nanofibers. Because of its excellent performance, it has been difficult to apply it to products that do not require electrical conduction.
  • An object of the present invention is to provide a carbon fiber composite material having a high volume resistivity, a manufacturing method thereof, an insulating article, an electronic component, and a logging apparatus.
  • the carbon fiber composite material according to the present invention is 20 parts by mass to 100 parts by mass of carbon nanofibers with reduced branch parts and oxidized with respect to 100 parts by mass of the elastomer,
  • the dynamic elastic modulus (E ′) at 200 ° C. and 10 Hz is 10 MPa to 1000 MPa,
  • the volume resistivity is 10 6 ⁇ ⁇ cm to 10 18 ⁇ ⁇ cm.
  • the carbon nanofibers can reduce branching portions by mechanical action before being blended with the elastomer.
  • the mechanical action can be done by a compression process.
  • the elastomer is a fluorine-containing elastomer
  • the dynamic elastic modulus (E ′) at 200 ° C. and 10 Hz is 15 MPa to 300 MPa
  • the volume resistivity value can be 10 11 ⁇ ⁇ cm to 10 18 ⁇ ⁇ cm.
  • the elastomer is ethylene-propylene rubber
  • the dynamic elastic modulus (E ′) at 200 ° C. and 10 Hz is 10 MPa to 200 MPa
  • the volume resistivity value can be 10 7 ⁇ ⁇ cm to 10 18 ⁇ ⁇ cm.
  • the mechanical action can be performed by a grinding process.
  • the elastomer is ethylene-propylene rubber
  • the dynamic elastic modulus (E ′) at 200 ° C. and 10 Hz is 10 MPa to 200 MPa
  • the volume resistivity value can be 10 8 ⁇ ⁇ cm to 10 18 ⁇ ⁇ cm.
  • the carbon nanofiber may have a maximum fiber length of less than 20 ⁇ m.
  • the insulating article for oil field according to the present invention may include the carbon fiber composite material.
  • the electronic component according to the present invention can include the insulating article.
  • the logging apparatus can include a casing and the electronic component disposed in the casing.
  • the method for producing a carbon fiber composite material according to the present invention includes: A step of obtaining a second carbon nanofiber by heat-treating the first carbon nanofiber produced by the vapor deposition method at a temperature higher than the reaction temperature in the vapor deposition method at 1100 ° C. to 1600 ° C. (A) and Treating the second carbon nanofibers by a mechanical action to reduce the branching portions of the second carbon nanofibers to obtain third carbon nanofibers; (C) a step of heat-treating the third carbon nanofibers in an atmosphere containing oxygen at 600 ° C. to 800 ° C. to obtain oxidized fourth carbon nanofibers; A step (d) of mixing the fourth carbon nanofibers with an elastomer and uniformly dispersing in the elastomer with a shearing force to obtain a carbon fiber composite material; including.
  • the heat treatment in the step (a) may be performed at 1200 ° C to 1500 ° C.
  • the third carbon nanofiber obtained in the step (b) may have a maximum fiber length of less than 20 ⁇ m.
  • the mechanical action of the step (b) is performed by a compression process,
  • the 3rd carbon nanofiber obtained by the said compression process can have no branch part.
  • the compression treatment can be performed by putting the second carbon nanofibers between at least two rotating rolls and applying a shearing force and a compressive force to the second carbon nanofibers.
  • the said compression process can use the binder for couple
  • the compression treatment can be performed with a dry compression granulator.
  • the mechanical action of the step (b) is performed by a pulverization process
  • the tap density of the third carbon nanofiber may be 1.5 to 10 times the tap density of the second carbon nanofiber.
  • the pulverization treatment can obtain the third carbon nanofiber having a nitrogen adsorption specific surface area of 1.1 to 5.0 times the nitrogen adsorption specific surface area of the second carbon nanofiber.
  • the pulverization treatment can be performed by dry pulverization using an impact and / or shear force.
  • the amount of increase in the oxygen concentration on the surface of the fourth carbon nanofiber relative to the oxygen concentration on the surface of the third carbon nanofiber measured by X-ray photoelectron spectroscopy (XPS) is 0.5 atm% to 2.6 atm. %.
  • the rate of increase in the oxygen concentration on the surface of the fourth carbon nanofiber relative to the oxygen concentration on the surface of the third carbon nanofiber measured by X-ray photoelectron spectroscopy (XPS) is 20% to 120%. Can do.
  • the fourth carbon nanofibers can be obtained by reducing the mass of the third carbon nanofibers by 2% to 20%.
  • the fourth carbon nanofiber obtained in the step (c) may have a surface oxygen concentration of 2.6 atm% to 4.6 atm% measured by X-ray photoelectron spectroscopy (XPS).
  • XPS X-ray photoelectron spectroscopy
  • the fourth carbon nanofiber obtained in the step (c) the ratio of the peak intensity D of around 1300 cm -1 to the peak intensity G of around 1600 cm -1 measured by Raman scattering spectroscopy (D / G) Can be 0.12 to 0.22.
  • the fourth carbon nanofiber obtained in the step (c) may have a nitrogen adsorption specific surface area of 45 m 2 / g to 60 m 2 / g.
  • the fourth carbon nanofiber obtained in the step (c) may have an average diameter of 70 nm to 100 nm.
  • FIG. 1A is a diagram schematically illustrating a second carbon nanofiber according to an embodiment of the present invention.
  • FIG. 1B is a diagram schematically illustrating a second carbon nanofiber according to an embodiment of the present invention.
  • FIG. 1C is a diagram schematically illustrating a second carbon nanofiber according to an embodiment of the present invention.
  • FIG. 1D is a diagram schematically illustrating a second carbon nanofiber according to an embodiment of the present invention.
  • FIG. 2 is a perspective view schematically showing the compression process in the step (b) according to the embodiment of the present invention.
  • FIG. 3 is a diagram schematically showing a second carbon nanofiber and a third carbon nanofiber according to an embodiment of the present invention.
  • FIG. 4 is a diagram schematically showing the step (d) by the open roll method according to the embodiment of the present invention.
  • FIG. 5 is a diagram schematically showing the step (d) by the open roll method according to the embodiment of the present invention.
  • FIG. 6 is a diagram schematically showing the step (d) by the open roll method according to the embodiment of the present invention.
  • FIG. 7 is a cross-sectional view schematically showing a logging tool for seabed use according to an embodiment of the present invention.
  • FIG. 8 is a cross-sectional view schematically showing a case of the logging apparatus in FIG. 7 according to one embodiment of the present invention.
  • FIG. 9 is a cross-sectional view schematically showing an underground logging tool according to an embodiment of the present invention.
  • the carbon fiber composite material according to an embodiment of the present invention includes 20 to 100 parts by mass of carbon nanofibers with reduced branching and oxidation with respect to 100 parts by mass of an elastomer, and dynamic elasticity at 200 ° C. and 10 Hz.
  • the rate (E ′) is 10 MPa to 1000 MPa, and the volume resistivity value is 10 6 ⁇ ⁇ cm to 10 18 ⁇ ⁇ cm.
  • An insulating article for use in oil fields according to an embodiment of the present invention may include the carbon fiber composite material.
  • An electronic component according to an embodiment of the present invention can include the insulating article.
  • the logging apparatus according to an embodiment of the present invention can include a housing and the electronic component disposed in the housing.
  • the first carbon nanofiber produced by the vapor deposition method is higher than the reaction temperature in the vapor deposition method, and 1100
  • Step (c) and the fourth carbon nanofibers are mixed with an elastomer and uniformly dispersed in the elastomer by a shearing force so as to be a carbon fiber composite material.
  • the carbon nanofiber will be described.
  • the fourth carbon nanofiber used in the present embodiment can be obtained by the steps (a) to (c) described below.
  • the untreated first carbon nanofibers manufactured by the vapor deposition method are heat-treated at a temperature higher than the reaction temperature in the vapor deposition method at 1100 ° C. to 1600 ° C.
  • the second carbon nanofiber can be obtained.
  • the temperature of this heat treatment is more preferably 1200 ° C. to 1500 ° C.
  • the surface structure of the first carbon nanofiber can be adjusted and surface defects can be reduced.
  • the heat treatment is performed at 1100 ° C.
  • the second carbon nanofibers obtained in this manner is heat treatment, for example, the ratio of the peak intensity D of around 1300 cm -1 to the peak intensity G of around 1600 cm -1 measured by Raman scattering spectroscopy (D / G ) Can be greater than 1.25 and less than 1.6.
  • the absorption peak intensity D of around 1300 cm -1 is the absorption based on defects in the crystal that forms the carbon nanofibers
  • the absorption peak intensity at around 1600 cm -1 G is carbon nanofiber Absorption based on crystals that form
  • the second carbon nanofiber having the ratio (D / G) of the peak intensity D to the peak intensity G within the above range has a non-crystalline portion on the surface, and thus has good wettability with the elastomer.
  • the strength of the second carbon nanofiber can be sufficient because there are relatively few defects.
  • the untreated carbon nanofibers produced by the vapor phase growth method are used. It is.
  • the untreated first carbon nanofibers produced by the vapor phase growth method are generally heat-treated at 2000 ° C. to 3200 ° C. in an inert gas atmosphere so-called graphitization (crystallization) treatment.
  • the second carbon nanofibers can be obtained by subjecting the first carbon nanofibers to the heat treatment of the step (a) at 1100 ° C. to 1600 ° C. sufficiently lower than the graphitization temperature without performing the graphitization treatment. it can.
  • the carbon fiber composite material using the second carbon nanofiber having a moderately amorphous portion on the surface has a volume compared to the carbon fiber composite material using the general graphitized carbon nanofiber. The specific resistance value can be increased.
  • the vapor phase growth method is also called a catalytic chemical vapor deposition (CCVD), in which a gas such as a hydrocarbon is pyrolyzed in the presence of a metal catalyst in the presence of a metal-based catalyst to perform untreated first carbon nano-particles.
  • CCVD catalytic chemical vapor deposition
  • a gas such as a hydrocarbon is pyrolyzed in the presence of a metal catalyst in the presence of a metal-based catalyst to perform untreated first carbon nano-particles.
  • a method of manufacturing a fiber will be described in more detail.
  • an organic compound such as benzene or toluene is used as a raw material
  • an organic transition metal compound such as ferrocene or nickelcene is used as a metal catalyst, and these are used together with a carrier gas at a high temperature such as 400 ° C.
  • a catalyst-supporting reaction method (Substrate Reaction Method) in which metal-containing particles supported on ceramics are brought into contact with a carbon-containing compound at a high temperature to generate first carbon nanofibers on a substrate can be used.
  • the average diameter of the untreated first carbon nanofibers obtained by such a vapor phase growth method can be 70 nm to 100 nm.
  • the aspect ratio of the first carbon nanofiber can be 50 to 200.
  • the average diameter and the average length of the carbon nanofibers are, for example, 5,000 times as many images as possible with an electron microscope (the magnification can be appropriately changed according to the size of the carbon nanofibers), and the average diameter and average of 200 or more locations. It can be obtained by measuring the length and calculating it as its arithmetic mean.
  • the first carbon nanofibers produced by the vapor deposition method include so-called carbon nanotubes.
  • the carbon nanotube has a structure in which one surface of graphite having a carbon hexagonal mesh surface is wound in one layer or multiple layers.
  • a carbon material partially having a carbon nanotube structure can also be used.
  • it may be called “graphite fibril nanotube” or “vapor-grown carbon fiber”.
  • FIG. 1A to 1D are views schematically showing a second carbon nanofiber according to an embodiment of the present invention.
  • the second carbon nanofiber 60 has substantially the same structure as the untreated first carbon nanofiber manufactured by the vapor deposition method, and is preferably linear in the longitudinal direction as shown in FIG. 1A. Is bent as shown in FIG. 1B, bent at the bent portion 62 as shown in FIG. 1C, and branched into a plurality (four in the figure) at the branch portion 64 as shown in FIG. 1D. Some of them are included.
  • the second carbon nanofiber 60 blended in the composite material is considered to be able to improve the flexibility and durability of the composite material in particular as it is linear as shown in FIG. 1A.
  • the second carbon nanofiber 60 as shown in 1D is considered to cause stress concentration at the bent portion 62 and the branching portion 64, and tends to reduce the original performance of the second carbon nanofiber as a reinforcing material in the composite material. It is thought that there is.
  • the bent portion 62 is a portion that is clearly bent as shown in FIG. 1C and does not include a bent portion as shown in FIG. 1B.
  • the second carbon nanofibers obtained in the step (a) are processed by a mechanical action to reduce the branch portions of the second carbon nanofibers, and the third carbon nanofibers are reduced. Nanofibers can be obtained.
  • the process by the mechanical action in the step (b) can be performed by a compression process or a pulverization process.
  • FIG. 2 is a perspective view schematically showing the step (b) according to the embodiment of the present invention. As shown in FIG.
  • the compression treatment is performed by introducing the second carbon nanofiber 60 as a raw material between a plurality of, for example, at least two rolls 72 and 74 that continuously rotate in the direction of the arrow in the drawing,
  • a dry compression granulator 70 such as a roll press machine or a roller compactor (roll type high pressure compression molding machine) that performs compression force on the first carbon nanofibers can be employed.
  • a plurality of second carbon nanofibers 60 obtained in the step (a) are put into a dry compression granulator 70 and compressed to obtain an aggregate of a plurality of third carbon nanofibers 80. it can.
  • the roll press machine normally uses a smooth roll that does not engrave pockets on the outer peripheral surface of the roll or a roll that engraves pockets.
  • the roll press machine is smooth to apply a compressive force evenly to the second carbon nanofibers.
  • a roll can be used.
  • the distance between the two rolls is set to 0 mm, that is, the rolls are in contact with each other, and a predetermined compression force F, for example, 980 to 2940 N / cm can be applied between the two rolls, and further 1500 to 2500 N / Cm is preferred.
  • the compressive force F can be set to an appropriate pressure while confirming the presence or absence of a branched portion in the obtained carbon nanofiber aggregate with an electron microscope or the like. If it is 980 N / cm or more, the 2nd carbon nanofiber which has a branch part can be cut
  • Such compression treatment can be performed a plurality of times, for example, about twice in order to homogenize the entire carbon nanofiber.
  • a binder such as water is generally blended to bind powder, but the compression treatment in the present embodiment is a dry granulation that does not use a binder for binding third carbon nanofibers. Can be. This is because if a binder is used, it may be difficult to disperse the fourth carbon nanofibers in a later step, and a step of removing the binder may be further required.
  • the powder is further crushed by a pulverizer or the like, An aggregate of carbon nanofibers 80 sized to a size can be produced.
  • the pulverizer at this time, for example, rotates the rotary blade at high speed and crushes the aggregate of carbon nanofibers 80 by the shearing force, and uses a screen to adjust the size only through the aggregate of carbon nanofibers 80 having an appropriate size or less. It can be performed.
  • FIG. 3 is a diagram schematically showing a third carbon nanofiber according to an embodiment of the present invention. As shown in FIG.
  • the second carbon nanofiber 60 having the branch part 64 shown on the upper left side of the figure is cut from the branch part 64 by the compression process, and for example 4 as shown on the lower right side of the figure.
  • a third carbon nanofiber 80 of the book is obtained. Therefore, the third carbon nanofibers 80 can reduce the number of branch portions 64 as compared with the second carbon nanofibers 60. In particular, even when observed with an electron microscope, the branch portions 64 can be eliminated.
  • the third carbon nanofiber having no branch portion becomes the fourth carbon nanofiber through the step (c), and the fourth carbon nanofiber in the composite material is mixed with other materials. Dispersibility can be improved, and flexibility and durability of the composite material can be improved.
  • the fourth carbon nanofiber does not have a branching portion, when it is compounded in the composite material, there is no stress concentration on the branching portion of the fourth carbon nanofiber, and as a reinforcing material for the fourth carbon nanofiber.
  • the performance degradation can be reduced. Since a part of the second carbon nanofiber having the bent part 62 as shown in FIG. 1C is also cut from the bent part 62, the second carbon nanofiber having the so-called defective part such as the bent part 62 and the branch part 64. 3 carbon nanofibers can be reduced.
  • the ratio of the third carbon nanofibers having the bent portions 62 may be less than 10 out of 100.
  • the 3rd carbon nanofiber 80 in which the defect parts like the bending part 62 and the branch part 64 reduced can have a maximum fiber length of less than 20 ⁇ m.
  • the maximum fiber length of carbon nanofibers is less than 20 ⁇ m, and more preferably less than 15 ⁇ m.
  • the flexibility of the composite material containing the fourth carbon nanofiber can be improved.
  • the plurality of third carbon nanofibers 80 may have a bulk density of 0.15 to 0.3 g / cm 3 . If the bulk density is 0.15 to 0.3 g / cm 3 , the third carbon nanofibers 80 are difficult to scatter and can be easily handled during storage, transportation or compounding, and handling properties are also good. Note that the bulk density in this application is JIS-K6219-2 carbon black for rubber-measurement of granulated particles-part 2 according to the measurement of bulk density, carbon nanofibers are poured into a 1000 cm 3 cylindrical container and the mass is calculated. Measured and obtained by calculating the bulk density (g / cm 3 ).
  • the plurality of third carbon nanofibers 80 obtained by the compression treatment is a set of a plurality of plate-like third carbon nanofibers in which a plurality of third carbon nanofibers gather to form a plate-like lump. Can be granulated in the body.
  • blending can be improved.
  • the tap density of the third carbon nanofibers obtained by the pulverization process in the step (b) is 1.5 to 10 times the tap density of the second carbon nanofibers obtained in the step (a). Can do.
  • the nitrogen adsorption specific surface area of the third carbon nanofiber can be 1.1 to 5.0 times the nitrogen adsorption specific surface area of the second carbon nanofiber before pulverization.
  • carbon nanofibers having improved surface reactivity with a matrix material such as an elastomer and improved wettability to the matrix material can be produced.
  • the second carbon nanofiber has defects such as a branched portion where the fiber is branched and a bent portion where the fiber is bent.
  • the surface of the carbon nanofiber is also activated. By reducing the defects, the carbon nanofibers are reduced in branching and bending portions, so that the strength of each fiber is improved and the fiber length is pulverized to such an extent that the fiber length is hardly reduced. Physical properties are improved.
  • Step (b) can be performed by dry grinding using impact and / or shearing force.
  • the dry pulverization can be performed in the absence of water or / and an organic solvent, for example. Dry pulverization is advantageous because there are no post-treatment steps such as removal of the dispersant after pulverization, drying of the solvent, and defibration of the dried and agglomerated fibers. Such dry pulverization can be performed at a peripheral speed of 50 to 200 m / s for 0.5 to 60 minutes.
  • a high-speed rotary mill, a ball mill, a medium stirring mill, a jet pulverizer, or the like can be used. A vibrating ball mill can be employed.
  • the second carbon nanofibers having the branch part are cut from the branch part, and the branch parts can be reduced, similarly to the compression process. Therefore, the pulverized third carbon nanofibers can have fewer branch portions than the second carbon nanofibers, and in particular, the branch portions can be eliminated even when observed with an electron microscope.
  • the tap density of the third carbon nanofibers after the pulverization process can be 1.5 to 10 times the second tap density before the pulverization process.
  • the third carbon nanofibers after the pulverization treatment can have a tap density of 0.03 to 0.2 g / cm 3 .
  • the tap density is an apparent density measured by the tap method, and represents the degree of bulk of the third carbon nanofiber. Therefore, if the branching locations and defects in the third carbon nanofibers are reduced by the pulverization process, the third carbon nanofibers tend to be densely packed and the tap density tends to increase.
  • the pulverized third carbon nanofibers having a tap density in the above range tend to have good wettability with a matrix material such as an elastomer.
  • the nitrogen adsorption specific surface area of the third carbon nanofibers after the pulverization treatment can be 1.1 to 5.0 times the nitrogen adsorption specific surface area of the second carbon nanofibers before the pulverization treatment.
  • the third carbon nanofiber after the pulverization treatment preferably has a nitrogen adsorption specific surface area of 22 to 100 m 2 / g.
  • the pulverized third carbon nanofiber having a nitrogen adsorption specific surface area in the above range tends to have good wettability with a matrix material such as an elastomer.
  • the third carbon nanofiber obtained in the step (b) is heat-treated at 600 ° C. to 800 ° C. in an oxygen-containing atmosphere to oxidize the fourth carbon nanofiber.
  • the third carbon nanofiber is placed in a furnace in an air atmosphere, set to a predetermined temperature in the temperature range of 600 ° C. to 800 ° C., and heat-treated, so that the surface has a desired oxygen concentration.
  • a fourth carbon nanofiber oxidized to can be obtained.
  • the heat treatment time in this step (c) is the time for holding the third carbon nanofibers in a heat treatment furnace at a predetermined temperature, and can be, for example, 10 minutes to 180 minutes.
  • the atmosphere containing oxygen may be air, an oxygen atmosphere, or an atmosphere in which an oxygen concentration is appropriately set.
  • heat treatment is performed depending on the content of the heat treatment furnace and the amount of the third carbon nanofiber to be treated.
  • the amount of oxygen introduced into the furnace can be adjusted as appropriate.
  • a sufficient oxygen concentration may be present in the atmosphere so that the surface of the fourth carbon nanofiber is oxidized to the desired oxygen concentration in the step (c).
  • the temperature of the heat treatment can be appropriately set in order to obtain a desired oxidation treatment in the range of 600 ° C to 800 ° C.
  • the heat treatment temperature and heat treatment time can be appropriately adjusted depending on the oxygen concentration in the furnace used in the step (c), the inner volume of the furnace, the amount of the third carbon nanofiber to be treated, and the like.
  • the heat treatment temperature in the present embodiment indicates the atmospheric temperature in the heat treatment furnace.
  • the increase in the oxygen concentration on the surface of the fourth carbon nanofiber relative to the oxygen concentration on the surface of the third carbon nanofiber measured by X-ray photoelectron spectroscopy (XPS) is 0.5 atm%.
  • the oxidation treatment can be performed so as to be ⁇ 2.6 atm%.
  • the amount of increase in the surface oxygen concentration of the fourth carbon nanofiber relative to the surface oxygen concentration of the third carbon nanofiber is 0.9 atm when the mechanical action in the step (b) is performed by the compression treatment. % To 2.6 atm%, and further 1.0 to 2.6 atm%, and 0.9 atm% when the mechanical action in the step (b) is performed by pulverization. It can be ⁇ 1.9 atm%, and further can be 1.0 atm% to 1.6 atm%.
  • the rate of increase in the oxygen concentration on the surface of the fourth carbon nanofiber relative to the oxygen concentration on the surface of the third carbon nanofiber measured by X-ray photoelectron spectroscopy (XPS) is 20%.
  • Oxidation treatment can be performed so as to be ⁇ 120%.
  • the increase ratio of the surface oxygen concentration of the fourth carbon nanofiber to the surface oxygen concentration of the third carbon nanofiber is 60% when the treatment by the mechanical action in the step (b) is performed by the compression treatment. 120%, and when the mechanical action in the step (b) is performed by pulverization, it can be 43% to 90%, and further can be 48% to 76%.
  • the surface oxygen concentration measured by X-ray photoelectron spectroscopy (XPS) of the fourth carbon nanofiber obtained in the step (c) can be 2.6 atm% to 4.6 atm%
  • the step (b ) In the case where the processing by the mechanical action is performed by the compression treatment, it can be 3.0 atm% to 4.6 atm%, and further can be 3.1 atm% to 4.6 atm%
  • step (b) In the case where the treatment by the mechanical action is performed by pulverization treatment, it can be 3.0 atm% to 4.0 atm%, and further can be 3.1 atm% to 3.7 atm%.
  • the surface of the third carbon nanofiber is appropriately oxidized to improve the surface reactivity between the fourth carbon nanofiber and the elastomer, thereby improving the dispersion of the carbon nanofiber in the elastomer. can do.
  • the mass of the fourth carbon nanofibers oxidized in the step (c) can be reduced by 2% to 20%, for example, from the mass of the third carbon nanofibers. It can be estimated that the fourth carbon nanofibers are appropriately oxidized. If the mass of the fourth carbon nanofiber is less than 2% less than the mass of the third carbon nanofiber, the oxygen concentration on the surface of the fourth carbon nanofiber is low, and it is difficult to improve the wettability. There is.
  • the 4th carbon nanofiber reduced in weight by more than 20% than the mass of the 3rd carbon nanofiber has a wettability almost the same as that of the 4th carbon nanofiber whose weight loss is 20% or less.
  • the loss due to the reduction of the carbon nanofibers due to the oxidation treatment is large, and it tends to be economically disadvantageous for the energy consumption of the heat treatment.
  • the surface of the third carbon nanofiber is oxidized, a part of the carbon on the surface of the third carbon nanofiber is vaporized as carbon dioxide gas to be reduced. It is preferable because it can be estimated that the length of the fourth carbon nanofiber does not become almost shorter unless the mass of the fourth carbon nanofiber exceeds 20% of the mass of the third carbon nanofiber.
  • the oxygen concentration on the surface of the fourth carbon nanofiber can be analyzed by XPS (X-ray photoelectron spectroscopy).
  • the analysis of the oxygen concentration by XPS is performed by, for example, argon gas for 0.5 minute to 1.0 minute with respect to the fourth carbon nanofiber before measurement in order to remove impurities attached to the surface of the fourth carbon nanofiber. It is preferable to perform analysis after etching to bring out the clean surface of the fourth carbon nanofiber.
  • the argon gas concentration of the argon gas etching can be 5 ⁇ 10 ⁇ 2 Pa to 20 ⁇ 10 ⁇ 2 Pa.
  • the analysis of the oxygen concentration by XPS is performed by attaching a carbon tape that is a conductive adhesive on a metal base of the XPS device, and then spraying the fourth carbon nanofiber on the carbon tape to adhere to the carbon tape, It can be performed in a state in which excess fourth carbon nanofibers not attached to the carbon tape are shaken off.
  • the analysis of the oxygen concentration by XPS the analysis can be performed in a state as close to powder as possible without pressing the fourth carbon nanofibers on the carbon tape and solidifying the block.
  • the third carbon nanofiber can be measured with an XPS apparatus.
  • the ratio of the peak intensity D of around 1300 cm -1 to the peak intensity G of around 1600 cm -1 measured by Raman scattering spectroscopy (D / G) is 0 .12 to 0.22.
  • the Raman peak ratio (D / G) of the fourth carbon nanofiber is larger than the Raman peak ratio (D / G) of the third carbon nanofiber because the crystal on the surface has many defects.
  • the fourth carbon nanofiber is desirably oxidized to such an extent that its Raman peak ratio (D / G) increases by 0.02 or more than the Raman peak ratio (D / G) of the third carbon nanofiber.
  • the fourth carbon nanofiber may have a nitrogen adsorption specific surface area of 34 m 2 / g to 58 m 2 / g.
  • the nitrogen adsorption specific surface area of the fourth carbon nanofiber is larger than the nitrogen adsorption specific surface area of the third carbon nanofiber because the surface thereof is rough.
  • the fourth carbon nanofiber is desirably oxidized to such an extent that its nitrogen adsorption specific surface area is increased by 9 m 2 / g or more from the nitrogen adsorption specific surface area of the third carbon nanofiber.
  • the average diameter of the fourth carbon nanofibers used in the step (c) is almost the same as the average diameter of the first carbon nanofibers.
  • the average diameter of the fourth carbon nanofibers obtained by such a vapor phase growth method can be 70 nm to 100 nm.
  • the surface reactivity with the elastomer is improved, the wettability to the elastomer can be improved, and the carbon fiber composite having a high volume resistivity and excellent electrical insulation performance.
  • Material can be obtained.
  • the blending amount of the fourth carbon nanofibers into the elastomer can be set according to the use. However, since the fourth carbon nanofibers have improved wettability with the elastomer, for example, carbon fibers having the same rigidity are used. When manufacturing a composite material, a compounding quantity can be reduced conventionally.
  • the elastomer may have a weight average molecular weight of 5,000 to 5,000,000, and further 20,000 to 3,000,000. When the molecular weight of the elastomer is within this range, the elastomer molecules are entangled with each other and are connected to each other. Therefore, the elastomer has good elasticity for dispersing the fourth carbon nanofibers.
  • the elastomer is preferable because it has a viscosity, so that the agglomerated fourth carbon nanofibers can easily enter each other, and the fourth carbon nanofibers can be separated from each other by having elasticity.
  • the elastomer has a spin-spin relaxation time (T2n / 30 ° C.) of the network component in the uncrosslinked body of 100 to 3000 ⁇ sec, measured at 30 ° C. by the Hahn echo method using pulsed NMR, and the observation nucleus is 1 H. Can be 200-1000 ⁇ s.
  • T2n / 30 ° C. spin-spin relaxation time
  • the elastomer can be flexible and have sufficiently high molecular mobility, that is, suitable for dispersing the fourth carbon nanofibers. It can have elasticity.
  • the elastomer has viscosity, when the elastomer and the fourth carbon nanofiber are mixed, the elastomer can easily enter the gap between the fourth carbon nanofibers due to high molecular motion. it can.
  • the elastomer has a network component spin-spin relaxation time (T2n) of 100 to 2000 ⁇ sec measured at 30 ° C. by the Hahn-echo method using pulsed NMR and the observation nucleus at 1 H. Can do.
  • T2n network component spin-spin relaxation time
  • the spin-spin relaxation time obtained by the Hahn-echo method using pulsed NMR is a measure representing the molecular mobility of a substance. Specifically, when the spin-spin relaxation time of the elastomer is measured by the Hahn-echo method using pulsed NMR, a first component having a first spin-spin relaxation time (T2n) having a short relaxation time, and relaxation A second component having a longer spin-spin relaxation time (T2nn) is detected.
  • the first component corresponds to a polymer network component (skeleton molecule), and the second component corresponds to a polymer non-network component (branch and leaf component such as a terminal chain).
  • the solid echo method As a measurement method in the pulse method NMR, the solid echo method, the CPMG method (Car Purcell, Mayboom, Gill method) or the 90 ° pulse method can be applied even if it is not the Hahn echo method.
  • the elastomer according to the present invention has a medium spin-spin relaxation time (T2), the Hahn echo method is most suitable.
  • the solid echo method and the 90 ° pulse method are suitable for short T2 measurement
  • the Hahn echo method is suitable for medium T2 measurement
  • the CPMG method is suitable for long T2 measurement.
  • the elastomer has an unsaturated bond or group having affinity for the radical at the end of the carbon nanofiber in at least one of the main chain, the side chain and the end chain, or generates such a radical or group.
  • unsaturated bonds or groups include double bonds, triple bonds, carbonyl groups, carboxyl groups, hydroxyl groups, amino groups, nitrile groups, ketone groups, amide groups, epoxy groups, ester groups, vinyl groups, halogen groups, It can be at least one selected from functional groups such as urethane groups, burette groups, allophanate groups and urea groups.
  • At least one of the main chain, side chain, and terminal chain of the elastomer has an unsaturated bond or group having high affinity (reactivity or polarity) with the radical of the carbon nanofiber, so that 4 carbon nanofibers can be bonded.
  • the radical of the carbon nanofiber so that 4 carbon nanofibers can be bonded.
  • elastomer natural rubber (NR), epoxidized natural rubber (ENR), styrene-butadiene rubber (SBR), nitrile rubber (NBR), chloroprene rubber (CR), ethylene-propylene rubber (EPR, EPDM), butyl rubber ( IIR), chlorobutyl rubber (CIIR), acrylic rubber (ACM), silicone rubber (Q), fluorine rubber (FKM), perfluoroelastomer (FFKM), butadiene rubber (BR), epoxidized butadiene rubber (EBR), epichlorohydrin rubber Elastomers such as (CO, CEO), urethane rubber (U), polysulfide rubber (T); olefin (TPO), polyvinyl chloride (TPVC), polyester (TPEE), polyurethane (TPU), polyamide (TPEA), Still System (SBS), thermoplastic elastomers, and the like; and may be a mixture thereof.
  • NR natural rubber
  • EDR epoxid
  • highly polar elastomers that easily generate free radicals during elastomer kneading, such as natural rubber (NR) and nitrile rubber (NBR).
  • NR natural rubber
  • NBR nitrile rubber
  • free radicals are generated by setting the kneading temperature at a relatively high temperature (for example, 50 ° C. to 150 ° C. in the case of EPDM).
  • a relatively high temperature for example, 50 ° C. to 150 ° C. in the case of EPDM.
  • the carbon fiber composite material which has a comparatively high volume specific resistance value can be obtained by mix
  • the elastomer may be either a rubber-based elastomer or a thermoplastic elastomer.
  • the elastomer may be either a crosslinked body or an uncrosslinked body.
  • a method for producing a carbon fiber composite material according to an embodiment of the present invention includes the first carbon nanofibers produced by the vapor deposition method in the vapor deposition method.
  • Including the step of obtaining the carbon fiber composite material is uniformly dispersed in the mer (d), the.
  • Steps (a) to (c) have been described in the above (I), and will be omitted.
  • Step (d) will be described in detail with reference to FIGS. 4 to 6 are diagrams schematically showing the step (d) by the open roll method according to the embodiment of the present invention. As shown in FIGS.
  • the first roll 10 and the second roll 20 in the two-roll open roll 2 are arranged at a predetermined interval d, for example, 0.5 mm to 1.5 mm. 4 to 6, the motor rotates in the direction indicated by the arrow at the rotational speeds V1 and V2 in the normal rotation or reverse rotation.
  • the elastomer 30 wound around the first roll 10 is masticated, and the elastomer molecular chain is appropriately cut to generate free radicals.
  • the free radicals of the elastomer generated by mastication are easily combined with the fourth carbon nanofibers obtained in the step (c).
  • FIG. 4 the motor rotates in the direction indicated by the arrow at the rotational speeds V1 and V2 in the normal rotation or reverse rotation.
  • the fourth carbon nanofibers 90 are put into the bank 34 of the elastomer 30 wound around the first roll 10 and kneaded.
  • the step of mixing the elastomer 30 and the fourth carbon nanofiber 90 is not limited to the open roll method, and for example, a closed kneading method or a multi-screw extrusion kneading method can also be used.
  • the roll interval d between the first roll 10 and the second roll 20 can be set to 0.5 mm or less, more preferably set to an interval of 0 to 0.5 mm.
  • the mixture 36 is put into the open roll 2 and thinning is performed once to several times. For example, the thinning can be performed about 1 to 10 times.
  • the ratio of the surface speeds (V1 / V2) in thinness is 1.05 to 3.00. Further, it can be 1.05 to 1.2.
  • a desired shear force can be obtained.
  • the carbon fiber composite material 50 extruded from between the narrow rolls as described above is greatly deformed as shown in FIG. 6 by the restoring force due to the elasticity of the elastomer 30, and the fourth carbon nanofiber 90 moves greatly together with the elastomer 30 at that time. To do.
  • the carbon fiber composite material 50 obtained through thinning is rolled with a roll and dispensed into a sheet having a predetermined thickness.
  • the roll temperature can be set to, for example, 0 to 50 ° C., and more preferably set to a relatively low temperature of 5 to 30 ° C.
  • the actually measured temperature of 30 can also be adjusted to 0 to 50 ° C. Due to the shearing force thus obtained, a high shearing force acts on the elastomer 30, and the aggregated fourth carbon nanofibers 90 are separated from each other so as to be pulled out one by one to the elastomer molecule. Distributed in.
  • the elastomer 30 has elasticity, viscosity, and chemical interaction with the fourth carbon nanofibers 90, the fourth carbon nanofibers 90 can be easily dispersed.
  • the carbon fiber composite material 50 excellent in the dispersibility and dispersion stability of the 4th carbon nanofiber 90 (it is hard to re-aggregate the 4th carbon nanofiber) can be obtained.
  • the viscous elastomer penetrates into the fourth carbon nanofiber, and a specific portion of the elastomer is chemically interlinked. By action, it binds to the highly active part of the fourth carbon nanofiber.
  • the surface of the fourth carbon nanofiber is moderately high by, for example, oxidation treatment, it can be easily bonded to an elastomer molecule.
  • the fourth carbon nanofibers move with the movement of the elastomer molecules, and further, the aggregated fourth carbon nanofibers are recovered by the restoring force of the elastomer due to elasticity after shearing.
  • the fibers will be separated and dispersed in the elastomer.
  • the carbon fiber composite material when the carbon fiber composite material is extruded from between narrow rolls, the carbon fiber composite material is deformed thicker than the roll interval due to the restoring force due to the elasticity of the elastomer. The deformation can be presumed to cause the carbon fiber composite material with a strong shear force to flow more complicatedly and disperse the fourth carbon nanofibers in the elastomer.
  • the fourth carbon nanofibers once dispersed are prevented from reaggregating due to chemical interaction with the elastomer, and can have good dispersion stability.
  • the step (d) of dispersing the fourth carbon nanofibers in the elastomer by a shearing force is not limited to the open roll method, and a closed kneading method or a multiaxial extrusion kneading method can also be used. In short, in this step, it is sufficient that a shearing force capable of separating the aggregated fourth carbon nanofibers can be given to the elastomer.
  • the open roll method can measure and manage the actual temperature of the mixture as well as the roll temperature.
  • a cross-linking carbon fiber composite material mixed with a cross-linking agent may be mixed and cross-linked to obtain a cross-linked carbon fiber composite material.
  • the carbon fiber composite material may be molded without being crosslinked.
  • the carbon fiber composite material may remain in the form of a sheet obtained by the open roll method, or a rubber molding process generally employed by the carbon fiber composite material obtained in the step (d), for example, injection molding method, transfer molding.
  • a desired shape such as a sheet may be formed by a method, a press molding method, an extrusion molding method, a calendering method, or the like.
  • a compounding agent usually used for processing an elastomer can be added.
  • a well-known thing can be used as a compounding agent.
  • the compounding agent examples include a crosslinking agent, a vulcanizing agent, a vulcanization accelerator, a vulcanization retarder, a softening agent, a plasticizer, a curing agent, a reinforcing agent, a filler, an antiaging agent, and a coloring agent. It can. These compounding agents can be added to the elastomer before the fourth carbon nanofibers in the open roll, for example.
  • the fourth carbon nanofiber is directly mixed with the elastomer having a rubber elasticity, but the present invention is not limited to this, and the following method is adopted.
  • the elastomer used as a raw material has a first spin-spin relaxation time (T2n) of the network component in an uncrosslinked body measured at 30 ° C. by a Hahn-echo method using pulsed NMR with an observation nucleus of 1 H. It is a rubber-like elastic body of 3000 ⁇ sec.
  • the raw material elastomer is masticated to lower the molecular weight of the elastomer, and a liquid elastomer having a first spin-spin relaxation time (T2n) exceeding 3000 ⁇ sec is obtained.
  • the first spin-spin relaxation time (T2n) of the liquid elastomer after mastication is 5 to 30 times the first spin-spin relaxation time (T2n) of the raw material elastomer before mastication. Can be.
  • This mastication is not suitable for kneading, unlike the general mastication performed while the elastomer remains in a solid state, by applying a strong shearing force by, for example, the open roll method to cut the molecular weight of the elastomer and significantly reduce the molecular weight.
  • the process is performed until the fluid reaches a certain level, for example, until it reaches a liquid state.
  • this mastication is performed at a roll temperature of 20 ° C. (minimum mastication time 60 minutes) to 150 ° C. (minimum mastication time 10 minutes), and the roll interval d is 0.5 mm to 1 for example.
  • the fourth carbon nanofibers are put into a liquid elastomer that is masticated at 0.0 mm.
  • the aggregated fourth carbon nanofibers are not dispersed so much even when kneaded in a state where the elastomer free radicals and the fourth carbon nanofibers are combined.
  • the fourth carbon nanofibers are uniformly dispersed in the elastomer by performing the thinning of the open roll method described in the above.
  • the mixture having an increased molecular weight of the elastomer has a first spin-spin relaxation time (T2n) of 3000 ⁇ sec or less as measured by a Hahn-echo method using pulsed NMR at 30 ° C. and an observation nucleus of 1 H. It is a rubber-like elastic body.
  • the first spin-spin relaxation time (T2n) of the rubber-like elastic mixture having an increased molecular weight of the elastomer is 0. It can be 5 to 10 times.
  • the elasticity of the rubber-like elastic mixture can be represented by the molecular form of the elastomer (observable by molecular weight) and molecular mobility (observable by T2n).
  • the step of increasing the molecular weight of the elastomer can be performed for 10 hours to 100 hours by placing the mixture in a heating furnace set to a heat treatment, for example, 40 ° C. to 100 ° C. By such a heat treatment, the molecular chain is extended by the bond between the free radicals of the elastomer present in the mixture, and the molecular weight is increased.
  • a small amount of a cross-linking agent for example, 1 ⁇ 2 or less of an appropriate amount of the cross-linking agent is mixed, and the mixture is subjected to a heat treatment (for example, an annealing treatment) to perform a cross-linking reaction.
  • the molecular weight can be increased in a short time.
  • the amount of crosslinking agent, the heating time, and the heating temperature can be set to such an extent that kneading is not difficult in the subsequent steps.
  • the fourth carbon nanofibers can be more uniformly dispersed in the elastomer by reducing the viscosity of the elastomer before introducing the fourth carbon nanofibers.
  • the fourth carbon is agglomerated by using a liquid elastomer having a reduced molecular weight, rather than mixing the fourth carbon nanofiber with an elastomer having a large molecular weight as in the production method described above.
  • the fourth carbon nanofibers can be dispersed more uniformly in the thinning process because it easily penetrates into the voids of the nanofibers.
  • the fourth carbon nanofibers are further bonded.
  • the fiber can be uniformly dispersed. Therefore, according to the step (d) described here, the same performance can be obtained with a small amount of the fourth carbon nanofiber than in the step (d) described above, and the expensive fourth carbon nanofiber is obtained. Saving money will also improve economic efficiency.
  • the carbon fiber composite material contains 20 to 100 parts by mass of carbon nanofibers that are reduced by mechanical action and oxidized to 100 parts by mass of the elastomer, and has a dynamic elastic modulus (E ′ at 200 ° C. and 10 Hz). ) Is 10 MPa to 1000 MPa, and the volume resistivity is 10 6 ⁇ ⁇ cm to 10 18 ⁇ ⁇ cm.
  • the carbon fiber composite material can include an elastomer and fourth carbon nanofibers uniformly dispersed in the elastomer.
  • elastomers and plastics have a volume resistivity exceeding 10 12 ( ⁇ ⁇ cm) at room temperature, and are highly insulating and have a volume resistivity of about 10 18 ( ⁇ ⁇ cm). Insulation.
  • carbon nanofibers that are commercially available, such as vapor-grown carbon fibers are uniformly dispersed in the elastomer and blended, even if the vapor-grown carbon fibers are relatively small, 10 1 ( ⁇ ⁇ cm) It has been found that it exhibits a volume resistivity value of some degree.
  • the volume resistivity value is a value measured by the four-probe method in accordance with JIS-7194 at room temperature.
  • the carbon fiber composite material in the present embodiment has a high volume resistivity value, even if a relatively large amount of the fourth carbon nanofiber is blended and evenly dispersed to obtain a desired strength, making it difficult to conduct electricity. Can be.
  • the carbon fiber composite material can have high strength and heat resistance due to the reinforcement of the carbon nanofibers, and can also be used for applications that require electrical insulation as a rubber material.
  • the required electrical insulation depends on the use of the rubber material, but for example, a volume resistivity value of 10 6 ( ⁇ ⁇ cm) or more may be required, and in particular, a volume resistivity value of 10 7 ( ⁇ ⁇ Cm) or more is often required, and can be applied to these applications.
  • Insulating articles for oil field applications can include carbon fiber composite materials.
  • the electronic component can include the insulating article.
  • the well logging apparatus can include a housing and the electronic component disposed in the housing.
  • the application requiring a volume resistivity of 10 6 ( ⁇ ⁇ cm) or more is effective, for example, in communication using an analog signal in a logging apparatus used in an oil field, and the volume resistivity is 10 7 ( ⁇ As an application requiring cm) or more, for example, it is effective in communication using a digital signal in a logging device, and in order to increase the communication speed, the volume specific resistance value should be 10 8 ( ⁇ ⁇ cm) or more. In particular, the volume resistivity value may be required to be 10 9 ( ⁇ ⁇ cm) or more.
  • the carbon fiber composite material has a volume resistivity value of 10 6 ⁇ ⁇ cm to 10 18 ⁇ ⁇ cm, and can be 10 7 ⁇ ⁇ cm to 10 18 ⁇ ⁇ cm, and more preferably 10 8 ⁇ ⁇ cm It can be 10 18 ⁇ ⁇ cm, in particular 10 9 ⁇ ⁇ cm to 10 18 ⁇ ⁇ cm.
  • a carbon fiber composite material using the fourth carbon nanofiber that has been subjected to compression treatment in the step (b) and a fluorine-containing elastomer as an elastomer has a dynamic elastic modulus (E ′) at 200 ° C.
  • the volume resistivity value can be 10 11 ⁇ ⁇ cm to 10 18 ⁇ ⁇ cm.
  • the carbon fiber composite material using the fourth carbon nanofiber that has been subjected to compression treatment in the step (b) and the ethylene-propylene rubber as the elastomer has a dynamic elastic modulus (E ′) at 200 ° C. of 10 MPa.
  • the volume resistivity value may be 10 7 ⁇ ⁇ cm to 10 18 ⁇ ⁇ cm.
  • the carbon fiber composite material using the fourth carbon nanofibers that have been pulverized in the step (b) and the ethylene-propylene rubber as the elastomer has a dynamic elastic modulus (E ′) at 200 ° C. of 10 MPa.
  • the volume resistivity value may be 10 8 ⁇ ⁇ cm to 10 18 ⁇ ⁇ cm.
  • the dynamic elastic modulus (E ′) is measured by performing a dynamic viscoelasticity test based on JIS K6394.
  • the carbon fiber composite material has a first spin-spin relaxation time (T2n) of 100 to 3000 ⁇ sec in a non-crosslinked body, measured at 150 ° C. by the Hahn echo method using pulsed NMR, and the observation nucleus is 1 H.
  • T2n and fnn measured at 150 ° C. of the carbon fiber composite material can represent that the fourth carbon nanofibers are uniformly dispersed in the matrix elastomer. That is, the fact that the fourth carbon nanofibers are uniformly dispersed in the elastomer can be said to be a state where the elastomer is constrained by the fourth carbon nanofibers.
  • the mobility of the elastomer molecules constrained by the fourth carbon nanofibers is smaller than that when not constrained by the fourth carbon nanofibers. Therefore, the first spin-spin relaxation time (T2n), the second spin-spin relaxation time (T2nn), and the spin-lattice relaxation time (T1) of the carbon fiber composite material do not include the fourth carbon nanofiber. It becomes shorter than the case of the elastomer alone, and particularly becomes shorter when the fourth carbon nanofibers are uniformly dispersed. In addition, in the state where the elastomer molecules are constrained by the fourth carbon nanofibers, it is considered that the non-network component (non-network chain component) decreases for the following reason.
  • the fourth carbon nanofibers are uniformly dispersed when the measurement value obtained by the Hahn echo method using the pulse method NMR is in the above range.
  • an elastomer molecule in which a part of the elastomer is subjected to molecular chain cleavage during kneading, and free radicals generated thereby attack and adsorb the surface of the fourth carbon nanofiber.
  • An interfacial phase that is considered to be an aggregate is formed.
  • the interfacial phase is considered to be similar to bound rubber formed around carbon black when, for example, an elastomer and carbon black are kneaded.
  • Such an interfacial phase is coated and protected by covering the fourth carbon nanofibers, and by blending more than a predetermined amount of carbon nanofibers, the interfacial phases are surrounded by an interfacial phase and divided into nanometer sizes. It is presumed to form small cells of the resulting elastomer. By forming such small cells almost uniformly throughout the carbon fiber composite material, it is possible to expect an effect that exceeds the effect of simply combining the two materials.
  • FIG. 7 is a cross-sectional view schematically showing a log logging device for seabed use according to an embodiment of the present invention.
  • FIG. 8 is a cross-sectional view schematically showing a case of the logging apparatus in FIG. 7 according to one embodiment of the present invention.
  • FIG. 9 is a cross-sectional view schematically showing an underground logging tool according to an embodiment of the present invention.
  • the logging tool is a physical property of the formation, oil layer, etc. in the borehole and around the well and the geometric properties of the well or casing (bore diameter, orientation, inclination, etc.) This is a device for recording the behavior of the oil layer flow for each depth, and can be used in, for example, an oil field.
  • Examples of the logging device for oil field use include a subsea application shown in FIGS. 7 and 8 and an underground application shown in FIG.
  • the logging equipment includes wireline logging (muline logging) and mud logging (mud logging), etc., and logging logging (LWD) with measuring equipment installed in the drilling assembly, While there is a measurement during excavation (MWD: Measurement While Drilling), a logging system used for wireline logging will be described here.
  • MWD Measurement While Drilling
  • a downhole apparatus 160 is entered as a logging apparatus, and the underground geological structure and the like are searched for, for example, the presence or absence of petroleum as a target material.
  • the downhole device 160 is fixed to, for example, the end of a long cable or communication link extending from the platform, and has a housing 161 such as a plurality of pressure vessels as shown in FIG.
  • the electronic equipment in the housing 161 is also required to have high heat resistance and high strength.
  • a plurality of electrical connectors 162 are arranged inside the housing 161, or the plurality of housings 161 are connected to each other by electrical connectors 162 formed in the end portions thereof.
  • the electrical connector 162 includes a plurality of pins 162a spaced apart from each other and a support portion 162b that fixes the plurality of pins 162a.
  • the support portion 162b can be formed of a carbon fiber composite material, for example, FIG.
  • the support portion 162b formed of a carbon fiber composite material like the electrical connectors 162 arranged at both ends of the casing 161.
  • the pin 162a of the electrical connector 162 is subjected to the vibration and impact of the downhole device 160, or when connected to the electric wire 163, the electric wire 163 vibrates due to the vibration, and thus the strength for securely fixing the pin 162a is required.
  • the pin 162a can be used for a relatively long time even in a severe environment at a high temperature in the well 156. It can have an insulation performance of 10 6 ( ⁇ ⁇ cm) or more, which is required between them.
  • the support portion 162 b of the electrical connector 162 can function as a feedthrough in the housing 161. Feedthroughs are shown, for example, in US Pat. No. 7,226,312 and are hereby incorporated by reference.
  • a plurality of electric wires 163 are arranged inside the housing 161 and connected to, for example, the pins 162 a of the electrical connector 162.
  • the electric wire 163 includes, for example, a conductive metal conductive wire as a core material and a covering portion covering the conductive wire, and the covering portion can be formed of a carbon fiber composite material.
  • the electric wire 163 covered with the carbon fiber composite material can withstand vibration and impact of the downhole device 160 under a severe environment at high temperature and can have insulation properties.
  • a cable 164 that is connected to the casing 161 and extends to the outside of the casing 161 and in which a plurality of core wires such as electric wires are bundled is disposed.
  • the cable 164 includes a core wire and a covering portion that covers the core wire, and the covering portion can be formed of a carbon fiber composite material.
  • the core wire of the cable 164 can be formed of a plurality of core wires, for example, electric wires.
  • Such a cable 164 has the role of transmitting and receiving data and commands between the case 161 in the underground and the data acquisition system on the ground and sending power to the electronic devices in the case 161 in the wireline logging. Can have.
  • Such a cable 164 can withstand abrasion and breakage due to contact with the inner surface of the rod extending into the well 156, and can have insulating properties. Cables are shown, for example, in US Pat. No. 7,259,331, which is hereby incorporated by reference. Further, for example, a plurality of coils 165 are arranged inside the housing 161, and a magnet wire is wound around these coils 165. The magnet wire is sometimes called a coil wire.
  • the magnet wire includes a conductive wire and a covering portion that covers the conductive wire, and the covering portion can be formed of a carbon fiber composite material.
  • the covering portion is formed as a thin insulating film by using a carbon fiber composite material, can withstand vibrations and impacts in a severe environment of high temperature of the downhole device 160, and can have insulating properties.
  • By covering the magnet wire with the carbon fiber composite material it is possible to effectively dissipate heat by the heat transfer effect of the fourth carbon nanofiber while maintaining the insulation.
  • Magnet wires are shown, for example, in US Pat. No. 6,898,997, incorporated herein by reference.
  • an electric board 166 on which a plurality of electronic components 167 are arranged, for example, is arranged inside the casing 161.
  • a heat dissipation sheet 167a can be disposed in order to prevent overheating due to self-heating of the plurality of electronic components 167, for example.
  • the heat dissipating sheet 167a is also called a heat sink, and is in contact with the surface of the electronic component 167, for example, and is disposed between the electronic component 167 and the electric board 166 in FIG. It can also be arranged so as to contact the surface of the electronic component 167.
  • the heat dissipation sheet 167a can be used as a vibration isolation sheet, and the impact resistance of the electronic component 167 can be improved.
  • the heat dissipation sheet is shown, for example, in US Patent Publication No. 2008/0223579, which is incorporated herein by reference. Isolation sheets are shown, for example, in U.S. Patent No. 6,280,874, U.S. Patent Publication No. 2009/0183941, and U.S. Patent Publication No. 2009/0151589, which are incorporated herein by reference.
  • the electronic component 167 arranged in the housing 161 and the electronic component (sensor 168) embedded in the wall portion 161a of the housing 161 can be encapsulated so as to cover the whole with a carbon fiber composite material.
  • the entire electronic component 167 can be waterproofed with the carbon fiber composite material.
  • the sensor 168 is disposed in the opening 168a formed in the wall portion 161a of the housing 161 together with the electric wire 163 including a lead wire (not shown) connected to the sensor 168, and the opening 168a is formed by the carbon fiber composite material 168b. Encapsulated (sometimes called mold).
  • the electronic component 167 may be enclosed in the carbon fiber composite material so as to cover the entire electronic component 167 on the electric substrate 166.
  • the sensor 168 and the electronic component 167 covered with the carbon fiber composite material 168b can have a waterproof structure against moisture inside the housing 161 and inside the housing 161, and can have insulating performance.
  • the blending amount of the fourth carbon nanofibers and other compounding agents such as carbon black can be appropriately blended according to the required performance such as strength and insulation in each component using the carbon fiber composite material.
  • 7 and 8 is an embodiment of the present invention, and in FIG. 8, a casing 161, an electrical connector 162, a cable 164, a coil 165, an electrical board 166, and a heat dissipation sheet 167a.
  • the waterproof structure is incorporated in one logging device has been described, the present invention is not limited to this, and the waterproof structure can be selected and incorporated according to the logging application. As shown in FIG.
  • the exploration of underground resources using wireline logging on the ground surface 153 is performed, for example, on the ground device 151 composed of a logging track 151a, a winch 151b, and the like, and from the winch 151b to the well 156.
  • it can be performed by a downhole apparatus 160 fixed to the tip of the extending wire line 155.
  • the downhole device 160 is basically the same as the logging device for the seabed application, and the description thereof is omitted here.
  • a spray nozzle is attached to the top of a vertical heating furnace (inner diameter 17.0 cm, length 150 cm).
  • the furnace wall temperature (reaction temperature) is raised to and maintained at 1000 ° C., and 20 g / min of a benzene liquid raw material containing 4% by weight of ferrocene is supplied from the spray nozzle at a flow rate of hydrogen gas of 100 L / min.
  • the shape of the spray at this time is a conical side surface (trumpet shape or umbrella shape), and the apex angle of the nozzle is 60 °.
  • ferrocene was pyrolyzed to produce iron fine particles, which became seeds, and the first carbon nanofibers were produced and grown from carbon obtained by pyrolysis of benzene.
  • the first carbon nanofibers grown by this method were continuously produced for 1 hour while scraping off at intervals of 5 minutes.
  • graphitized carbon nanofibers shown as “S” in the table
  • pulverized carbon nanofibers shown as “SH” in the table
  • Oxidized carbon nanofibers shown as “SO” in the table
  • the graphitized carbon nanofiber (S) was graphitized by further heat-treating the first carbon nanofiber obtained in (1-1) above at 2800 ° C. in an inert gas atmosphere.
  • the graphitized carbon nanofiber (S) had an average diameter of 87 nm, an average length of 9.1 ⁇ m, and a surface oxygen concentration of 2.1 atm%.
  • the graphitized carbon nanofiber (S) is a commercially available carbon nanofiber, and is a trade name VGCF-S manufactured by Showa Denko K.K.
  • SH pulverized carbon nanofiber
  • the graphitized carbon nanofiber (S) was put into a rotary pulverizer Wonder Blender WB-1 (stainless steel pulverization blade, peripheral speed 180 m / s) manufactured by Osaka Chemical Co., Ltd. Obtained by grinding for 5 minutes.
  • Oxidation treated carbon nanofiber (SO) is a heating furnace (size is 700 mm) in which 120 g of graphitized carbon nanofiber (S) is put in a container (size is 300 mm ⁇ 300 mm ⁇ 150 mm) and air atmosphere is continuously introduced at 50 ml / min. ⁇ 350 mm ⁇ 900 mm), and obtained by performing an oxidation treatment by holding in a heating furnace at a heat treatment temperature and a heat treatment time in the step (c) shown in Table 1 and performing a heat treatment.
  • the actual temperature in the heating furnace was in the range of ⁇ 30 ° C. with respect to the set temperature.
  • the fourth carbon nanofiber (shown as “SAPO” in the table) using the compression treatment in step (b) is the first carbon nanofiber obtained in (1-1),
  • a second carbon nanofiber (SA) is obtained by heat treatment at a heat treatment temperature (1200 ° C.) of step (a) shown in Table 1 which is lower than the reaction temperature in the vapor phase growth method in an inert gas atmosphere,
  • the second carbon nanofiber (SA) is put into a dry compression granulator having two rolls and the roll treatment in the step (b) shown in Table 1 is performed to obtain a third carbon nanofiber (SAP).
  • the third carbon nanofiber (SAP) is put in a heating furnace in an air atmosphere, and is held in the heating furnace at a heat treatment temperature (650 ° C.) and a heat treatment time (2 hours) in step (c) shown in Table 1. Oxidation treatment by heat treatment Give me.
  • the roll process of the process (b) in manufacture of a 4th carbon nanofiber was obtained by throwing the 2nd carbon nanofiber (SA) into the dry compression granulator which has two rolls.
  • the dry compression granulator is a roll press (roll diameter is 150 mm, roll is smooth roll, roll interval is 0 mm, set compression force between rolls (linear pressure) is 1960 N / cm, gear ratio is 1: 1.3, roll rotation Several rpm).
  • the roll-treated carbon nanofiber was granulated into a plate-like lump (carbon nanofiber aggregate) having a diameter of about 2 to 3 cm.
  • the granulated plate-like lump was further crushed through a crushing and granulating machine (rotation speed: 15 rpm, screen: 5 mm) having eight rotary blades to adjust the particle size.
  • the oxidation treatment in the step (c) in the production of the fourth carbon nanofiber was the same as the production conditions of the oxidation treatment carbon nanofiber (SO), description thereof is omitted here.
  • the fourth carbon nanofiber (shown as “SAHO” in the table) using the pulverization treatment in step (b) is the same as the first carbon nanofiber obtained in (1-1) above in an inert gas atmosphere.
  • the second carbon nanofiber (SA) is obtained by heat treatment at the heat treatment temperature (1200 ° C.) of step (a) shown in Table 1 which is lower than the reaction temperature in the vapor phase growth method.
  • the fiber (SA) was put into a rotary pulverizer wonder blender WB-1 (stainless steel pulverizing blade, peripheral speed 180 m / s) manufactured by Osaka Chemical Co.
  • WB-1 stainless steel pulverizing blade, peripheral speed 180 m / s
  • a third carbon nanofiber (SAH) is obtained, and the third carbon nanofiber (SAH) is placed in a heating furnace in an air atmosphere, and the heat treatment temperature (650 ° C.) and heat treatment time in step (c) shown in Table 1 Held in a heating furnace obtained by performing an oxidation process by heat treatment for 2 hours).
  • the grinding process of the process (b) in manufacture of a 4th carbon nanofiber is the same as the manufacturing conditions of the said grinding
  • the measurement of the bulk density is sometimes called a zero tap density, and was measured according to JIS-K6219-2.
  • the measurement of the fiber length and the ratio of having defects are performed by taking 40 field images of carbon nanofibers at a magnification of 5000 with a scanning electron microscope (SEM), and 50 fiber lengths for a total of 200 fibers for each field of view. And the number of fibers having defects was determined by measurement. Defects count the number of fibers having branched portions and bent portions, respectively, and the ratio of defects (branched portions and bent portions) is the ratio (%) that the number of fibers having each defect is included in 200. Calculated.
  • the ratio of carbon nanofibers having a maximum fiber length of 20 ⁇ m or more (shown as “a ratio of 20 ⁇ m or more” in Table 1) was calculated.
  • the measurement of the remaining mass ratio of the fourth carbon nanofiber (SAPO) is the ratio of the mass of the fourth carbon nanofiber (SAPO) when the mass of the third carbon nanofiber (SAP) is 100 mass%. Was defined as the remaining mass rate.
  • the measurement of the remaining mass ratio of the fourth carbon nanofiber (SAHO) is the ratio of the mass of the fourth carbon nanofiber (SAHO) when the mass of the third carbon nanofiber (SAH) is 100 mass%.
  • the remaining mass rate is the remaining mass ratio of the fourth carbon nanofiber (SAHO) when the mass of the third carbon nanofiber (SAH) is 100 mass%.
  • the measurement of the residual mass ratio of oxidized carbon nanofibers is based on the ratio of the mass of oxidized carbon nanofibers (SO) when the mass of graphitized carbon nanofibers (S) is 100% by mass.
  • the residual mass rate was assumed.
  • Measurement of the Raman peak ratio KAISER OPTICAL SYSTEM Co. HOLOLAB-5000 Type: peak intensity at around 1300 cm -1 by Raman scattering spectroscopy using a (532nmND YAG) to the peak intensity G in the vicinity of 1600 cm -1 in each carbon nanofiber The ratio of D (D / G) was measured.
  • the nitrogen adsorption specific surface area was measured by measuring the nitrogen adsorption specific surface area (m 2 / g) of each carbon nanofiber using NOVA3000 type (nitrogen gas) manufactured by Yuasa Ionics. Although not shown in the table, the nitrogen adsorption specific surface area of the third carbon nanofiber (SAH) was 38 (m 2 / g).
  • the measurement of the oxygen concentration was performed using XPS (third carbon nanofiber (SAP or SAH), graphitized carbon nanofiber (S), oxidized carbon nanofiber (SO) and fourth carbon nanofiber (SAPO or SAHO). It measured using the X-ray photoelectron spectroscopy (X-ray Photoelectron Spectroscopy). Specifically, for example, the fourth carbon nanofiber will be described.
  • the fourth carbon nanofiber is sprinkled on the carbon tape on the metal base to adhere to the carbon tape, and the extra carbon nanofiber that has not adhered to the carbon tape is first attached.
  • the fourth carbon nanofiber was shaken off and a metal base was mounted in the XPS apparatus.
  • XPS apparatus “X-ray photoelectron spectrometer JPS-9200 for micro analysis (hereinafter referred to as XPS apparatus) manufactured by JEOL Ltd. was used.
  • a fourth carbon nanofiber as a powder sample was used.
  • Argon gas etching was performed at an argon gas concentration of 8 ⁇ 10 ⁇ 2 Pa for 0.5 minutes to bring out a clean surface of the fourth carbon nanofiber, and the X-ray source of the XPS apparatus had an analysis diameter of 1 mm and a counter cathode.
  • the oxygen concentration on the surface of the fourth carbon nanofiber was measured by setting an Al / Mg twin target, an acceleration voltage of 10 kV, and an emission current of 30 mA.
  • the elements on the surface of the fourth carbon nanofiber detected by XPS were oxygen and The same measurement was performed on other carbon nanofibers.
  • the fourth carbon nanofiber (SAPO) of the fourth carbon nanofiber (SAPO) with respect to the surface oxygen concentration ( ap ) of the third carbon nanofiber (SAP) before the oxidation treatment is performed.
  • Examples of Examples 1 to 2 and Comparative Examples 1 to 5 are open rolls having a roll diameter of 6 inches ( 100 parts by mass (phr) of a fluorine-containing elastomer (“FKM”) shown in Tables 2 and 3 was added to a roll temperature of 10 to 20 ° C. and wound around a roll.
  • FKM fluorine-containing elastomer
  • each carbon nanofiber obtained in (1) in parts by mass (phr) shown in Tables 2 and 3 was added to the elastomer together with compounding agents such as triallyl isocyanate and peroxide. At this time, the roll gap was set to 1.5 mm.
  • the mixture containing the compounding agent was taken out from the roll.
  • the roll gap was narrowed from 1.5 mm to 0.3 mm, and the mixture was further introduced into the roll for thinning.
  • the surface speed ratio of the two rolls was set to 1.1. Thinning was repeated 10 times.
  • a roll was set in a predetermined gap (1.1 mm), a thin composite material was charged, and dispensed to obtain a non-crosslinked carbon fiber composite material.
  • the carbon fiber composite material thus obtained was rolled with a roll, press-molded (cured) at 170 ° C. for 10 minutes, and further post-cured at 200 ° C. for 24 hours.
  • Examples 1-2 and Comparative Example 1 A crosslinked carbon fiber composite material (sheet shape having a thickness of 1 mm) was obtained.
  • “FKM” in Tables 2 and 4 is Viton GF-600S (a weight average molecular weight of 50,000, T2n / 30 ° C. is 50 ⁇ sec), a ternary fluorine-containing elastomer manufactured by DuPont Dow Elastomer Japan. there were.
  • the surface speed ratio of the two rolls was set to 1.1. Furthermore, the carbon fiber composite material obtained by setting the roll gap to 1.1 mm and passing through was put and dispensed. The separated sheets were compression molded at 90 ° C. for 5 minutes to obtain uncrosslinked carbon fiber composite material samples of Examples 3 to 8 and Comparative Examples 6 to 9 having a thickness of 1 mm. Further, 2 parts by mass of peroxide (phr) was mixed with the non-crosslinked carbon fiber composite material obtained through thinning, and the mixture was put into an open roll having a roll gap set to 1.1 mm and dispensed.
  • peroxide peroxide
  • Carbon fiber composite material containing peroxide that was dispensed and cut into a mold size was set in a mold, compression molded at 175 ° C., 100 kgf / cm 2 for 20 minutes, and Examples 3 to 5 having a thickness of 1 mm and comparison
  • the crosslinked carbon fiber composite material samples of Examples 6 to 8 were obtained.
  • EPDM was the trade name EP103AF of ethylene-propylene rubber manufactured by JSR.
  • Comparative Examples 1 and 6 carbon nanofibers were not blended, but the same kneading process was performed.
  • the first spin-spin relaxation time (T2n / 150 ° C.) and the component fraction (fnn) of the component having the second spin-spin relaxation time were determined for each sample.
  • the measurement results are shown in Tables 2-4.
  • the first spin-spin relaxation times (T2n / 30 ° C.) of the raw rubber measured in the same manner are also shown in Tables 2 to 5. Note that the carbon fiber composite material samples of Examples 1 to 5, 7, and 8 were affected by the magnetic field generated by the carbon nanofibers and could not be measured.
  • a tensile test was performed based on JIS K6251 at a tensile speed of 500 mm / min, and tensile strength (TB (MPa)), elongation at break (EB (%)) and 100% stress (M100) were measured.
  • a dynamic viscoelasticity test made by SII Co., Ltd. was performed on test pieces obtained by cutting the carbon fiber composite material samples of the crosslinked bodies of Examples 1 to 8 and Comparative Examples 1 to 9 into strips (40 ⁇ 1 ⁇ 5 (width) mm).
  • the electrical insulation of the carbon fiber composite material sample is evaluated. If the volume resistivity is 1 ⁇ 10 6 or more, the insulation is good (shown as “ ⁇ ” in the table), and the volume is specific. If the resistance value is less than 1 ⁇ 10 6 , the insulation is low (shown as “x” in the table).
  • the crosslinked carbon fiber composite material containing the fourth carbon nanofibers of Examples 1 and 2 is more in comparison with the carbon fiber composite materials of Comparative Examples 1 to 5. Even when a large amount of the fourth carbon nanofiber was blended, the volume resistivity was high and the electrical insulation was good.
  • the crosslinked carbon fiber composite material containing the fourth carbon nanofibers of Examples 3 to 8 contains a larger amount of the fourth carbon nanofiber than the carbon fiber composite materials of Comparative Examples 6 to 9. Even so, the volume resistivity was high and the electrical insulation was good.

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Abstract

Disclosed is a carbon-fiber composite material which comprises 100 parts by mass of an elastomer (30) and 20-100 parts by mass of carbon nanofibers (90) that have a reduced content of branches and have been oxidized. The carbon-fiber composite material (50) has a dynamic modulus (E') at 200ºC and 10 Hz of 10-1,000 MPa and a volume resistivity of 106-1018 O·cm.

Description

炭素繊維複合材料及びその製造方法、絶縁性物品、電子部品、及び検層装置Carbon fiber composite material and manufacturing method thereof, insulating article, electronic component, and logging device

 本発明は、炭素繊維複合材料及びその製造方法、絶縁性物品、電子部品、及び検層装置に関する。 The present invention relates to a carbon fiber composite material and a manufacturing method thereof, an insulating article, an electronic component, and a logging apparatus.

 カーボンナノファイバーは、機械的特性に優れ、複合材料として様々な分野でその応用が期待されている。特に、カーボンナノファイバーは電気伝導性にも優れているので、カーボンナノファイバーをエラストマー中に均一に分散した炭素繊維複合材料は例えば電子放出装置へ応用することも提案されている(例えば、特開2008−311083号公報)。 Carbon nanofibers are excellent in mechanical properties and are expected to be applied in various fields as composite materials. In particular, since carbon nanofibers are also excellent in electrical conductivity, it has been proposed that a carbon fiber composite material in which carbon nanofibers are uniformly dispersed in an elastomer is applied to, for example, an electron emission device (for example, JP 2008-311083).

 また、エラストマーにカーボンナノファイバーを配合した複合材料は、機械的特性に優れているため、従来のゴム製品の代替品としての様々な用途へも期待されている。しかしながら、このような従来のゴム製品の中にはゴムの絶縁性を利用した製品も少なくないが、カーボンナノファイバーを均一に分散させた炭素繊維複合材料は少量のカーボンナノファイバーの配合でも電気伝導性にも優れるため、電気伝導を望まない製品への適用は難しかった。 Also, composite materials in which carbon nanofibers are blended with elastomers are excellent in mechanical properties, and thus are expected to be used in various applications as substitutes for conventional rubber products. However, many of these conventional rubber products use the insulating properties of rubber, but carbon fiber composites with uniformly dispersed carbon nanofibers can conduct electricity even with a small amount of carbon nanofibers. Because of its excellent performance, it has been difficult to apply it to products that do not require electrical conduction.

 本発明の目的は、体積固有抵抗値の高い炭素繊維複合材料及びその製造方法、絶縁性物品、電子部品、及び検層装置を提供することにある。 An object of the present invention is to provide a carbon fiber composite material having a high volume resistivity, a manufacturing method thereof, an insulating article, an electronic component, and a logging apparatus.

 本発明にかかる炭素繊維複合材料は、
 エラストマー100質量部に対して、分岐部を減らしかつ酸化したカーボンナノファイバーを20質量部~100質量部含み、
 200℃、10Hzにおける動的弾性率(E’)が10MPa~1000MPaであって、
 体積固有抵抗値が10Ω・cm~1018Ω・cmである。
The carbon fiber composite material according to the present invention is
20 parts by mass to 100 parts by mass of carbon nanofibers with reduced branch parts and oxidized with respect to 100 parts by mass of the elastomer,
The dynamic elastic modulus (E ′) at 200 ° C. and 10 Hz is 10 MPa to 1000 MPa,
The volume resistivity is 10 6 Ω · cm to 10 18 Ω · cm.

 本発明にかかる炭素繊維複合材料において、
 前記カーボンナノファイバーは、前記エラストマーに配合される前に、機械的作用により分岐部を減らすことができる。
In the carbon fiber composite material according to the present invention,
The carbon nanofibers can reduce branching portions by mechanical action before being blended with the elastomer.

 本発明にかかる炭素繊維複合材料において、
 前記機械的作用は、圧縮処理によってなされることができる。
In the carbon fiber composite material according to the present invention,
The mechanical action can be done by a compression process.

 本発明にかかる炭素繊維複合材料において、
 前記エラストマーが含フッ素エラストマーであって、
 200℃、10Hzにおける動的弾性率(E’)が15MPa~300MPaであって、
 体積固有抵抗値が1011Ω・cm~1018Ω・cmであることができる。
In the carbon fiber composite material according to the present invention,
The elastomer is a fluorine-containing elastomer,
The dynamic elastic modulus (E ′) at 200 ° C. and 10 Hz is 15 MPa to 300 MPa,
The volume resistivity value can be 10 11 Ω · cm to 10 18 Ω · cm.

 本発明にかかる炭素繊維複合材料において、
 前記エラストマーがエチレン−プロピレンゴムであって、
 200℃、10Hzにおける動的弾性率(E’)が10MPa~200MPaであって、
 体積固有抵抗値が10Ω・cm~1018Ω・cmであることができる。
In the carbon fiber composite material according to the present invention,
The elastomer is ethylene-propylene rubber,
The dynamic elastic modulus (E ′) at 200 ° C. and 10 Hz is 10 MPa to 200 MPa,
The volume resistivity value can be 10 7 Ω · cm to 10 18 Ω · cm.

 本発明にかかる炭素繊維複合材料において、
 前記機械的作用は、粉砕処理によってなされることができる。
In the carbon fiber composite material according to the present invention,
The mechanical action can be performed by a grinding process.

 本発明にかかる炭素繊維複合材料において、
 前記エラストマーがエチレン−プロピレンゴムであって、
 200℃、10Hzにおける動的弾性率(E’)が10MPa~200MPaであって、
 体積固有抵抗値が10Ω・cm~1018Ω・cmであることができる。
In the carbon fiber composite material according to the present invention,
The elastomer is ethylene-propylene rubber,
The dynamic elastic modulus (E ′) at 200 ° C. and 10 Hz is 10 MPa to 200 MPa,
The volume resistivity value can be 10 8 Ω · cm to 10 18 Ω · cm.

 本発明にかかる炭素繊維複合材料において、
 前記カーボンナノファイバーは、最大繊維長が20μm未満であることができる。
In the carbon fiber composite material according to the present invention,
The carbon nanofiber may have a maximum fiber length of less than 20 μm.

 本発明にかかる油田用途の絶縁性物品は、前記炭素繊維複合材料を含むことができる。 The insulating article for oil field according to the present invention may include the carbon fiber composite material.

 本発明にかかる電子部品は、前記絶縁性物品を含むことができる。 The electronic component according to the present invention can include the insulating article.

 本発明にかかる検層装置は、筐体と、該筐体内に配置された前記電子部品と、を備えることができる。 The logging apparatus according to the present invention can include a casing and the electronic component disposed in the casing.

 本発明にかかる炭素繊維複合材料の製造方法は、
 気相成長法によって製造された第1のカーボンナノファイバーを、前記気相成長法における反応温度より高温であって、かつ、1100℃~1600℃で熱処理して第2のカーボンナノファイバーを得る工程(a)と、
 前記第2のカーボンナノファイバーを機械的作用によって処理して、第2のカーボンナノファイバーの分岐部を減らして、第3のカーボンナノファイバーを得る工程(b)と、
 前記第3のカーボンナノファイバーを酸素を含有する雰囲気中で600℃~800℃で熱処理して、酸化した第4のカーボンナノファイバーを得る工程(c)と、
 前記第4のカーボンナノファイバーを、エラストマーに混合し、剪断力で該エラストマー中に均一に分散して炭素繊維複合材料を得る工程(d)と、
 を含む。
The method for producing a carbon fiber composite material according to the present invention includes:
A step of obtaining a second carbon nanofiber by heat-treating the first carbon nanofiber produced by the vapor deposition method at a temperature higher than the reaction temperature in the vapor deposition method at 1100 ° C. to 1600 ° C. (A) and
Treating the second carbon nanofibers by a mechanical action to reduce the branching portions of the second carbon nanofibers to obtain third carbon nanofibers;
(C) a step of heat-treating the third carbon nanofibers in an atmosphere containing oxygen at 600 ° C. to 800 ° C. to obtain oxidized fourth carbon nanofibers;
A step (d) of mixing the fourth carbon nanofibers with an elastomer and uniformly dispersing in the elastomer with a shearing force to obtain a carbon fiber composite material;
including.

 本発明にかかる炭素繊維複合材料の製造方法において、
 前記工程(a)の前記熱処理は、1200℃~1500℃であることができる。
In the method for producing a carbon fiber composite material according to the present invention,
The heat treatment in the step (a) may be performed at 1200 ° C to 1500 ° C.

 本発明にかかる炭素繊維複合材料の製造方法において、
 前記工程(b)で得られた前記第3のカーボンナノファイバーは、最大繊維長が20μm未満であることができる。
In the method for producing a carbon fiber composite material according to the present invention,
The third carbon nanofiber obtained in the step (b) may have a maximum fiber length of less than 20 μm.

 本発明にかかる炭素繊維複合材料の製造方法において、
 前記工程(b)の前記機械的作用は、圧縮処理によってなされ、
 前記圧縮処理によって得られた第3のカーボンナノファイバーは、分岐部を有しないことができる。
In the method for producing a carbon fiber composite material according to the present invention,
The mechanical action of the step (b) is performed by a compression process,
The 3rd carbon nanofiber obtained by the said compression process can have no branch part.

 本発明にかかる炭素繊維複合材料の製造方法において、
 前記圧縮処理は、少なくとも2本の回転するロール間に前記第2のカーボンナノファイバーを投入して、前記第2のカーボンナノファイバーに剪断力と圧縮力とを加えることによって行われることができる。
In the method for producing a carbon fiber composite material according to the present invention,
The compression treatment can be performed by putting the second carbon nanofibers between at least two rotating rolls and applying a shearing force and a compressive force to the second carbon nanofibers.

 本発明にかかる炭素繊維複合材料の製造方法において、
 前記圧縮処理は、カーボンナノファイバー同士を結合するためのバインダーを用いないことができる。
In the method for producing a carbon fiber composite material according to the present invention,
The said compression process can use the binder for couple | bonding carbon nanofibers.

 本発明にかかる炭素繊維複合材料の製造方法において、
 前記圧縮処理は、乾式圧縮造粒機で行われることができる。
In the method for producing a carbon fiber composite material according to the present invention,
The compression treatment can be performed with a dry compression granulator.

 本発明にかかる炭素繊維複合材料の製造方法において、
 前記工程(b)の前記機械的作用は、粉砕処理によってなされ、
 前記第3のカーボンナノファイバーのタップ密度は、前記第2のカーボンナノファイバーのタップ密度の1.5倍~10倍であることができる。
In the method for producing a carbon fiber composite material according to the present invention,
The mechanical action of the step (b) is performed by a pulverization process,
The tap density of the third carbon nanofiber may be 1.5 to 10 times the tap density of the second carbon nanofiber.

 本発明にかかる炭素繊維複合材料の製造方法において、
 前記粉砕処理は、前記第2のカーボンナノファイバーの窒素吸着比表面積の1.1倍~5.0倍の窒素吸着比表面積を有する前記第3のカーボンナノファイバーを得ることができる。
In the method for producing a carbon fiber composite material according to the present invention,
The pulverization treatment can obtain the third carbon nanofiber having a nitrogen adsorption specific surface area of 1.1 to 5.0 times the nitrogen adsorption specific surface area of the second carbon nanofiber.

 本発明にかかる炭素繊維複合材料の製造方法において、
 前記粉砕処理は、衝撃及び/または剪断力を利用した乾式粉砕で行なうことができる。
In the method for producing a carbon fiber composite material according to the present invention,
The pulverization treatment can be performed by dry pulverization using an impact and / or shear force.

 本発明にかかる炭素繊維複合材料の製造方法において、
 X線光電子分光法(XPS)で測定した、前記第3のカーボンナノファイバーの表面の酸素濃度に対する前記第4のカーボンナノファイバーの表面の酸素濃度の増加量は、0.5atm%~2.6atm%であることができる。
In the method for producing a carbon fiber composite material according to the present invention,
The amount of increase in the oxygen concentration on the surface of the fourth carbon nanofiber relative to the oxygen concentration on the surface of the third carbon nanofiber measured by X-ray photoelectron spectroscopy (XPS) is 0.5 atm% to 2.6 atm. %.

 本発明にかかる炭素繊維複合材料の製造方法において、
 X線光電子分光法(XPS)で測定した、前記第3のカーボンナノファイバーの表面の酸素濃度に対する前記第4のカーボンナノファイバーの表面の酸素濃度の増加割合は、20%~120%であることができる。
In the method for producing a carbon fiber composite material according to the present invention,
The rate of increase in the oxygen concentration on the surface of the fourth carbon nanofiber relative to the oxygen concentration on the surface of the third carbon nanofiber measured by X-ray photoelectron spectroscopy (XPS) is 20% to 120%. Can do.

 本発明にかかる炭素繊維複合材料の製造方法において、
 前記工程(c)の熱処理は、前記第3のカーボンナノファイバーの質量を2%~20%減量して前記第4のカーボンナノファイバーを得ることができる。
In the method for producing a carbon fiber composite material according to the present invention,
In the heat treatment in the step (c), the fourth carbon nanofibers can be obtained by reducing the mass of the third carbon nanofibers by 2% to 20%.

 本発明にかかる炭素繊維複合材料の製造方法において、
 前記工程(c)で得られた前記第4のカーボンナノファイバーは、X線光電子分光法(XPS)で測定した表面の酸素濃度が2.6atm%~4.6atm%であることができる。
In the method for producing a carbon fiber composite material according to the present invention,
The fourth carbon nanofiber obtained in the step (c) may have a surface oxygen concentration of 2.6 atm% to 4.6 atm% measured by X-ray photoelectron spectroscopy (XPS).

 本発明にかかる炭素繊維複合材料の製造方法において、
 前記工程(c)で得られた前記第4のカーボンナノファイバーは、ラマン散乱分光法によって測定される1600cm−1付近のピーク強度Gに対する1300cm−1付近のピーク強度Dの比(D/G)が0.12~0.22であることができる。
In the method for producing a carbon fiber composite material according to the present invention,
The fourth carbon nanofiber obtained in the step (c) the ratio of the peak intensity D of around 1300 cm -1 to the peak intensity G of around 1600 cm -1 measured by Raman scattering spectroscopy (D / G) Can be 0.12 to 0.22.

 本発明にかかる炭素繊維複合材料の製造方法において、
 前記工程(c)で得られた前記第4のカーボンナノファイバーは、窒素吸着比表面積が45m/g~60m/gであることができる。
In the method for producing a carbon fiber composite material according to the present invention,
The fourth carbon nanofiber obtained in the step (c) may have a nitrogen adsorption specific surface area of 45 m 2 / g to 60 m 2 / g.

 本発明にかかる炭素繊維複合材料の製造方法において、
 前記工程(c)で得られた前記第4のカーボンナノファイバーは、平均直径が70nm~100nmであることができる。
In the method for producing a carbon fiber composite material according to the present invention,
The fourth carbon nanofiber obtained in the step (c) may have an average diameter of 70 nm to 100 nm.

図1Aは、本発明の一実施形態にかかる第2のカーボンナノファイバーを模式的に示す図である。FIG. 1A is a diagram schematically illustrating a second carbon nanofiber according to an embodiment of the present invention. 図1Bは、本発明の一実施形態にかかる第2のカーボンナノファイバーを模式的に示す図である。FIG. 1B is a diagram schematically illustrating a second carbon nanofiber according to an embodiment of the present invention. 図1Cは、本発明の一実施形態にかかる第2のカーボンナノファイバーを模式的に示す図である。FIG. 1C is a diagram schematically illustrating a second carbon nanofiber according to an embodiment of the present invention. 図1Dは、本発明の一実施形態にかかる第2のカーボンナノファイバーを模式的に示す図である。FIG. 1D is a diagram schematically illustrating a second carbon nanofiber according to an embodiment of the present invention. 図2は、本発明の一実施形態にかかる工程(b)の圧縮処理を模式的に示す斜視図である。FIG. 2 is a perspective view schematically showing the compression process in the step (b) according to the embodiment of the present invention. 図3は、本発明の一実施形態にかかる第2のカーボンナノファイバーと第3のカーボンナノファイバーとを模式的に示す図である。FIG. 3 is a diagram schematically showing a second carbon nanofiber and a third carbon nanofiber according to an embodiment of the present invention. 図4は、本発明の一実施形態にかかるオープンロール法による工程(d)を模式的に示す図である。FIG. 4 is a diagram schematically showing the step (d) by the open roll method according to the embodiment of the present invention. 図5は、本発明の一実施形態にかかるオープンロール法による工程(d)を模式的に示す図である。FIG. 5 is a diagram schematically showing the step (d) by the open roll method according to the embodiment of the present invention. 図6は、本発明の一実施形態にかかるオープンロール法による工程(d)を模式的に示す図である。FIG. 6 is a diagram schematically showing the step (d) by the open roll method according to the embodiment of the present invention. 図7は、本発明の一実施形態にかかる海底用途の検層装置を模式的に示す断面図である。FIG. 7 is a cross-sectional view schematically showing a logging tool for seabed use according to an embodiment of the present invention. 図8は、本発明の一実施形態にかかる図7における検層装置の筐体を模式的に示す断面図である。FIG. 8 is a cross-sectional view schematically showing a case of the logging apparatus in FIG. 7 according to one embodiment of the present invention. 図9は、本発明の一実施形態にかかる地下用途の検層装置を模式的に示す断面図である。FIG. 9 is a cross-sectional view schematically showing an underground logging tool according to an embodiment of the present invention.

 以下、本発明の実施の形態について、詳細に説明する。 Hereinafter, embodiments of the present invention will be described in detail.

 本発明の一実施形態にかかる炭素繊維複合材料は、エラストマー100質量部に対して、分岐部を減らしかつ酸化したカーボンナノファイバーを20質量部~100質量部含み、200℃、10Hzにおける動的弾性率(E’)が10MPa~1000MPaであって、体積固有抵抗値が10Ω・cm~1018Ω・cmである。本発明の一実施形態にかかる油田用途の絶縁性物品は、前記炭素繊維複合材料を含むことができる。本発明の一実施形態にかかる電子部品は、前記絶縁性物品を含むことができる。本発明の一実施形態にかかる検層装置は、筐体と、該筐体内に配置された前記電子部品と、を備えることができる。本発明の一実施形態にかかる炭素繊維複合材料の製造方法は、気相成長法によって製造された第1のカーボンナノファイバーを、前記気相成長法における反応温度より高温であって、かつ、1100℃~1600℃で熱処理して第2のカーボンナノファイバーを得る工程(a)と、前記第2のカーボンナノファイバーを機械的作用によって処理して、第2のカーボンナノファイバーの分岐部を減らして、第3のカーボンナノファイバーを得る工程(b)と、前記第3のカーボンナノファイバーを酸素を含有する雰囲気中で600℃~800℃で熱処理して、酸化した第4のカーボンナノファイバーを得る工程(c)と、前記第4のカーボンナノファイバーを、エラストマーに混合し、剪断力で該エラストマー中に均一に分散して炭素繊維複合材料を得る工程(d)と、を含む。 The carbon fiber composite material according to an embodiment of the present invention includes 20 to 100 parts by mass of carbon nanofibers with reduced branching and oxidation with respect to 100 parts by mass of an elastomer, and dynamic elasticity at 200 ° C. and 10 Hz. The rate (E ′) is 10 MPa to 1000 MPa, and the volume resistivity value is 10 6 Ω · cm to 10 18 Ω · cm. An insulating article for use in oil fields according to an embodiment of the present invention may include the carbon fiber composite material. An electronic component according to an embodiment of the present invention can include the insulating article. The logging apparatus according to an embodiment of the present invention can include a housing and the electronic component disposed in the housing. In the method for producing a carbon fiber composite material according to an embodiment of the present invention, the first carbon nanofiber produced by the vapor deposition method is higher than the reaction temperature in the vapor deposition method, and 1100 A step (a) of obtaining a second carbon nanofiber by heat treatment at from 1 to 1600 ° C., and treating the second carbon nanofiber by a mechanical action to reduce the number of branches of the second carbon nanofiber. And (b) obtaining third carbon nanofibers, and heat treating the third carbon nanofibers in an atmosphere containing oxygen at 600 ° C. to 800 ° C. to obtain oxidized fourth carbon nanofibers. Step (c) and the fourth carbon nanofibers are mixed with an elastomer and uniformly dispersed in the elastomer by a shearing force so as to be a carbon fiber composite material. A step of obtaining (d), including.

 (I)カーボンナノファイバー
カーボンナノファイバーについて説明する。
本実施の形態に用いる第4のカーボンナノファイバーは、以下に説明する工程(a)~工程(c)によって得ることができる。
まず、工程(a)として、気相成長法によって製造された未処理の第1のカーボンナノファイバーを、前記気相成長法における反応温度より高温であって、かつ、1100℃~1600℃で熱処理して第2のカーボンナノファイバーを得ることができる。この熱処理の温度は、1200℃~1500℃であることがさらに好ましい。工程(a)における熱処理の温度が気相成長法の反応温度より高温であることで、第1のカーボンナノファイバーの表面構造を整え、表面の欠陥を減少させることができる。また、この熱処理が1100℃~1600℃とすることで、マトリックス材料例えばエラストマーとの表面反応性が向上し、マトリックス材料中におけるカーボンナノファイバーの分散不良をより改善することができる。このように熱処理されて得られた第2のカーボンナノファイバーは、例えば、ラマン散乱分光法によって測定される1600cm−1付近のピーク強度Gに対する1300cm−1付近のピーク強度Dの比(D/G)が1.25を超えかつ1.6未満であることができる。第2のカーボンナノファイバーのラマンスペクトルにおいて、1300cm−1付近の吸収ピーク強度Dはカーボンナノファイバーを形成する結晶内の欠陥に基づく吸収であり、1600cm−1付近の吸収ピーク強度Gはカーボンナノファイバーを形成する結晶に基づく吸収である。このため、ピーク強度Dとピーク強度Gとの比(D/G)が小さい程、カーボンナノファイバーの結晶化程度が高いことを示す。したがって、ピーク強度Gに対するピーク強度Dの比(D/G)が小さいほどグラファイト化(黒鉛化)度が高く、表面に欠陥の少ないカーボンナノファイバーを意味する。したがって、前記範囲のピーク強度Gに対するピーク強度Dの比(D/G)を有する第2のカーボンナノファイバーは、適度に表面に非結晶部分が存在するため、エラストマーとの濡れ性が良好であり、比較的欠陥も少ないので第2のカーボンナノファイバーの強度も十分であることができる。なお、ここで、第1のカーボンナノファイバーは、工程(a)~工程(c)における熱処理や圧縮処理などを受けていないため、気相成長法によって製造されたままの未処理のカーボンナノファイバーである。このように気相成長法で製造された未処理の第1のカーボンナノファイバーは、一般的には、不活性ガス雰囲気中において2000℃~3200℃で熱処理していわゆる黒鉛化(結晶化)処理されて、気相成長の際に第1のカーボンナノファイバーの表面に沈積したアモルファス状の堆積物や残留している触媒金属などの不純物を除去されるが、本実施形態においては、このような黒鉛化処理を行うことなく、第1のカーボンナノファイバーを黒鉛化処理の温度よりも十分に低い1100℃~1600℃で工程(a)の熱処理を行って第2のカーボンナノファイバーを得ることができる。このように、適度に表面に非晶質部分が存在する第2のカーボンナノファイバーを用いた炭素繊維複合材料は、一般的な黒鉛化されたカーボンナノファイバーを用いた炭素繊維複合材料に比べ体積固有抵抗値が高くなることができる。
(I) Carbon nanofiber The carbon nanofiber will be described.
The fourth carbon nanofiber used in the present embodiment can be obtained by the steps (a) to (c) described below.
First, as the step (a), the untreated first carbon nanofibers manufactured by the vapor deposition method are heat-treated at a temperature higher than the reaction temperature in the vapor deposition method at 1100 ° C. to 1600 ° C. Thus, the second carbon nanofiber can be obtained. The temperature of this heat treatment is more preferably 1200 ° C. to 1500 ° C. When the temperature of the heat treatment in the step (a) is higher than the reaction temperature of the vapor phase growth method, the surface structure of the first carbon nanofiber can be adjusted and surface defects can be reduced. In addition, when the heat treatment is performed at 1100 ° C. to 1600 ° C., the surface reactivity with the matrix material such as an elastomer is improved, and poor dispersion of the carbon nanofibers in the matrix material can be further improved. The second carbon nanofibers obtained in this manner is heat treatment, for example, the ratio of the peak intensity D of around 1300 cm -1 to the peak intensity G of around 1600 cm -1 measured by Raman scattering spectroscopy (D / G ) Can be greater than 1.25 and less than 1.6. In the Raman spectrum of the second carbon nanofibers, the absorption peak intensity D of around 1300 cm -1 is the absorption based on defects in the crystal that forms the carbon nanofibers, the absorption peak intensity at around 1600 cm -1 G is carbon nanofiber Absorption based on crystals that form For this reason, the smaller the ratio (D / G) between the peak intensity D and the peak intensity G, the higher the degree of crystallization of the carbon nanofibers. Therefore, the smaller the ratio of the peak intensity D to the peak intensity G (D / G), the higher the degree of graphitization (graphitization), and the carbon nanofibers with fewer defects on the surface. Therefore, the second carbon nanofiber having the ratio (D / G) of the peak intensity D to the peak intensity G within the above range has a non-crystalline portion on the surface, and thus has good wettability with the elastomer. The strength of the second carbon nanofiber can be sufficient because there are relatively few defects. Here, since the first carbon nanofibers are not subjected to the heat treatment or compression treatment in the steps (a) to (c), the untreated carbon nanofibers produced by the vapor phase growth method are used. It is. In general, the untreated first carbon nanofibers produced by the vapor phase growth method are generally heat-treated at 2000 ° C. to 3200 ° C. in an inert gas atmosphere so-called graphitization (crystallization) treatment. Thus, impurities such as amorphous deposits and remaining catalytic metals deposited on the surface of the first carbon nanofibers during vapor phase growth are removed. In the present embodiment, such an impurity is removed. The second carbon nanofibers can be obtained by subjecting the first carbon nanofibers to the heat treatment of the step (a) at 1100 ° C. to 1600 ° C. sufficiently lower than the graphitization temperature without performing the graphitization treatment. it can. As described above, the carbon fiber composite material using the second carbon nanofiber having a moderately amorphous portion on the surface has a volume compared to the carbon fiber composite material using the general graphitized carbon nanofiber. The specific resistance value can be increased.

 気相成長法は、触媒気相合成法(Catalytic Chemical Vapor Deposition:CCVD)とも呼ばれ、炭化水素等のガスを金属系触媒の存在下で気相熱分解させて未処理の第1のカーボンナノファイバーを製造する方法である。より詳細に気相成長法を説明すると、例えば、ベンゼン、トルエン等の有機化合物を原料とし、フェロセン、ニッケルセン等の有機遷移金属化合物を金属系触媒として用い、これらをキャリアーガスとともに高温例えば400℃~1000℃の反応温度に設定された反応炉に導入し、浮遊状態あるいは反応炉壁に第1のカーボンナノファイバーを生成させる浮遊流動反応法(Floating Reaction Method)や、あらかじめアルミナ、酸化マグネシウム等のセラミックス上に担持された金属含有粒子を炭素含有化合物と高温で接触させて第1のカーボンナノファイバーを基板上に生成させる触媒担持反応法(Substrate Reaction Method)等を用いることができる。このような気相成長法で得られた未処理の第1のカーボンナノファイバーの平均直径は、70nm~100nmであることができる。また、第1のカーボンナノファイバーのアスペクト比は50~200であることができる。本発明の詳細な説明においてカーボンナノファイバーの平均直径及び平均長さは、電子顕微鏡による例えば5,000倍の撮像(カーボンナノファイバーのサイズによって適宜倍率は変更できる)から200箇所以上の直径及び平均長さを計測し、その算術平均値として計算して得ることができる。
気相成長法によって製造された第1のカーボンナノファイバーは、例えば、いわゆるカーボンナノチューブなどが例示できる。カーボンナノチューブは、炭素六角網面のグラファイトの1枚面を1層もしくは多層に巻いた構造を有する。また、部分的にカーボンナノチューブの構造を有する炭素材料も使用することができる。なお、カーボンナノチューブという名称の他にグラファイトフィブリルナノチューブ、気相成長炭素繊維といった名称で称されることもある。
The vapor phase growth method is also called a catalytic chemical vapor deposition (CCVD), in which a gas such as a hydrocarbon is pyrolyzed in the presence of a metal catalyst in the presence of a metal-based catalyst to perform untreated first carbon nano-particles. A method of manufacturing a fiber. The vapor phase growth method will be described in more detail. For example, an organic compound such as benzene or toluene is used as a raw material, an organic transition metal compound such as ferrocene or nickelcene is used as a metal catalyst, and these are used together with a carrier gas at a high temperature such as 400 ° C. It is introduced into a reaction furnace set to a reaction temperature of ~ 1000 ° C, and the floating reaction method (floating reaction method) in which a first carbon nanofiber is generated in a floating state or on the reaction furnace wall, or alumina, magnesium oxide, etc. A catalyst-supporting reaction method (Substrate Reaction Method) in which metal-containing particles supported on ceramics are brought into contact with a carbon-containing compound at a high temperature to generate first carbon nanofibers on a substrate can be used. The average diameter of the untreated first carbon nanofibers obtained by such a vapor phase growth method can be 70 nm to 100 nm. The aspect ratio of the first carbon nanofiber can be 50 to 200. In the detailed description of the present invention, the average diameter and the average length of the carbon nanofibers are, for example, 5,000 times as many images as possible with an electron microscope (the magnification can be appropriately changed according to the size of the carbon nanofibers), and the average diameter and average of 200 or more locations. It can be obtained by measuring the length and calculating it as its arithmetic mean.
Examples of the first carbon nanofibers produced by the vapor deposition method include so-called carbon nanotubes. The carbon nanotube has a structure in which one surface of graphite having a carbon hexagonal mesh surface is wound in one layer or multiple layers. A carbon material partially having a carbon nanotube structure can also be used. In addition to the name “carbon nanotube”, it may be called “graphite fibril nanotube” or “vapor-grown carbon fiber”.

 図1A~図1Dは、本発明の一実施形態にかかる第2のカーボンナノファイバーを模式的に示す図である。
第2のカーボンナノファイバー60は、気相成長法によって製造された未処理の第1のカーボンナノファイバーと概略同じ構造であって、図1Aに示すように長手方向に直線的であることが好ましいが、図1Bに示すように湾曲しているもの、図1Cに示すように折曲部62で折れ曲っているもの、図1Dに示すように分岐部64で複数(図では4本)に枝分かれしているものもある程度含まれる。複合材料に配合された第2のカーボンナノファイバー60は、図1Aのように直線的である程、特に複合材料の柔軟性や耐久性を向上させることができると考えられるが、図1C、図1Dに示すような第2のカーボンナノファイバー60は、折曲部62や分岐部64において応力集中が起きると考えられ、複合材料における補強材としての第2のカーボンナノファイバー本来の性能を減じる傾向があると考えられる。なお、折曲部62は、図1Cに示すように明確に折れ曲っている箇所であって、図1Bのように湾曲しているものは含まない。
1A to 1D are views schematically showing a second carbon nanofiber according to an embodiment of the present invention.
The second carbon nanofiber 60 has substantially the same structure as the untreated first carbon nanofiber manufactured by the vapor deposition method, and is preferably linear in the longitudinal direction as shown in FIG. 1A. Is bent as shown in FIG. 1B, bent at the bent portion 62 as shown in FIG. 1C, and branched into a plurality (four in the figure) at the branch portion 64 as shown in FIG. 1D. Some of them are included. The second carbon nanofiber 60 blended in the composite material is considered to be able to improve the flexibility and durability of the composite material in particular as it is linear as shown in FIG. 1A. The second carbon nanofiber 60 as shown in 1D is considered to cause stress concentration at the bent portion 62 and the branching portion 64, and tends to reduce the original performance of the second carbon nanofiber as a reinforcing material in the composite material. It is thought that there is. The bent portion 62 is a portion that is clearly bent as shown in FIG. 1C and does not include a bent portion as shown in FIG. 1B.

 次に、工程(b)は、前記工程(a)で得られた第2のカーボンナノファイバーを機械的作用によって処理して、第2のカーボンナノファイバーの分岐部を減らして、第3のカーボンナノファイバーを得ることができる。
工程(b)における機械的作用による処理は、圧縮処理または粉砕処理によって行うことができる。
Next, in the step (b), the second carbon nanofibers obtained in the step (a) are processed by a mechanical action to reduce the branch portions of the second carbon nanofibers, and the third carbon nanofibers are reduced. Nanofibers can be obtained.
The process by the mechanical action in the step (b) can be performed by a compression process or a pulverization process.

 まず、圧縮処理を用いた工程(b)について説明する。
工程(b)における圧縮処理によって得られた第3のカーボンナノファイバーは、分岐部を有しないことができる。工程(b)における圧縮処理は、第2のカーボンナノファイバーを少なくとも分岐部から切断するための高い圧力が必要である。ここでは、工程(b)について、図2を用いて詳細に説明する。図2は、本発明の一実施形態にかかる工程(b)を模式的に示す斜視図である。図2に示すように、圧縮処理は、図中の矢印方向に連続回転する複数例えば少なくとも2本のロール72,74間に原料である第2のカーボンナノファイバー60を投入して、剪断力と圧縮力とを第1のカーボンナノファイバーに加えることによって行う、例えばロールプレス機やローラーコンパクター(ロール式高圧圧縮成形機)のような乾式圧縮造粒機70を採用することができる。工程(a)によって得られた複数の第2のカーボンナノファイバー60を乾式圧縮造粒機70に投入して圧縮処理することで、複数の第3のカーボンナノファイバー80の集合体を得ることができる。ロールプレス機は、通常ロール外周面にポケットを刻まない平滑ロールまたはポケットを刻んだロール等を使用するが、本実施の形態においては第2のカーボンナノファイバーに均等に圧縮力を加えるために平滑ロールを用いることができる。また、2本のロールの間隔は0mmすなわちロール同士が接触するように設定され、さらに2本のロール間には所定の圧縮力F例えば980~2940N/cmを与えることができ、さらに1500~2500N/cmを与えることが好ましい。圧縮力Fは、得られたカーボンナノファイバー集合体における分岐部の有無を電子顕微鏡などで確認しながら適当な圧力に設定することができる。980N/cm以上であれば分岐部を有する第2のカーボンナノファイバーを分岐部で切断することができる。このような圧縮処理は、カーボンナノファイバー全体の均質化のため、複数回例えば2回程度行うことができる。造粒機では、一般に粉体を結合するために水などのバインダーを配合するが、本実施の形態における圧縮処理は、第3のカーボンナノファイバー同士を結合するためのバインダーを用いない乾式造粒であることができる。バインダーを用いると、後工程で第4のカーボンナノファイバーを分散させにくくする虞があり、バインダーを除去する工程がさらに必要になることがあるためである。
なお、通常であれば乾式圧縮造粒機70によって2本のロール間で圧縮して板状(フレーク)のカーボンナノファイバー80の集合体に成形した後、さらに粉砕機などで破砕し、所望の大きさに整粒したカーボンナノファイバー80の集合体をつくることができる。このときの粉砕機は、例えば回転刃を高速回転させてその剪断力によりカーボンナノファイバー80の集合体を破砕し、スクリーンを用いて適当なサイズ以下のカーボンナノファイバー80の集合体だけを通して整粒を行うことができる。圧縮処理だけではカーボンナノファイバー80の集合体の大きさにばらつきが大きいが、このようにさらに破砕することでカーボンナノファイバー80の集合体の粒径が適度な大きさに整えられるため、マトリックス材料と混練した時のカーボンナノファイバーの集合体の偏りを防ぐことができる。この圧縮処理によって第3のカーボンナノファイバーが分岐部で切断され、ふわりとしない所望の嵩密度になって取り扱いが容易になり、例えば板状の第3のカーボンナノファイバー集合体に造粒されることができる。
圧縮処理することによって得られた第3のカーボンナノファイバーについて図3を用いて詳細に説明する。図3は、本発明の一実施形態にかかる第3のカーボンナノファイバーを模式的に示す図である。
図3に示すように、圧縮処理によって、図の左上側に示した分岐部64を有する第2のカーボンナノファイバー60が分岐部64から切断され、図の右下側に示したように例えば4本の第3のカーボンナノファイバー80が得られる。したがって、第3のカーボンナノファイバー80は、第2のカーボンナノファイバー60よりも分岐部64を減らすことができ、特に、電子顕微鏡で観察しても分岐部64がなくなることができる。このように分岐部が無い第3のカーボンナノファイバーは、工程(c)を経て第4のカーボンナノファイバーとなって他の材料と混合したときにも複合材料中の第4のカーボンナノファイバーの分散性を向上させることができ、また、複合材料の柔軟性や耐久性を向上させることができる。さらに、第4のカーボンナノファイバーにも分岐部がないので、複合材料に配合した際に、第4のカーボンナノファイバーの分岐部への応力集中がなく、第4のカーボンナノファイバーの補強材としての性能低下を減少することができる。図1Cで示したような折曲部62を有する第2のカーボンナノファイバーの一部も折曲部62から切断されるため、折曲部62や分岐部64のようないわゆる欠陥部分を有する第3のカーボンナノファイバーを減少させることができる。圧縮処理によって得られた第3のカーボンナノファイバー80の内、折曲部62を有する第3のカーボンナノファイバーを含む割合が100本中10本未満であることができる。折曲部62を有する第3のカーボンナノファイバーを含む割合が100本中10本以上であると、圧縮処理によって十分に欠陥部分を除去できていない可能性がある。このように折曲部62や分岐部64のような欠陥部分が減少した第3のカーボンナノファイバー80は、最大繊維長が20μm未満であることができる。近年、市場の要求としてカーボンナノファイバーの最大繊維長が20μm未満、さらに15μm未満であることが好ましいとされることがある。例えば、第3のカーボンナノファイバーの最大繊維長を20μm未満とすることで、第4のカーボンナノファイバーを配合した複合材料の柔軟性を向上することができる。複数の第3のカーボンナノファイバー80は、嵩密度が0.15~0.3g/cmであることができる。嵩密度が0.15~0.3g/cmであれば第3のカーボンナノファイバー80が飛散しにくく保管時、運搬時または配合時における扱いが容易になってハンドリング性も良好である。なお、本願における嵩密度は、JIS−K6219−2ゴム用カーボンブラック−造粒粒子の測定−第2部かさ密度の測定にしたがって、1000cmの円筒容器にカーボンナノファイバーを注ぎ落としてその質量を測定し、嵩密度(g/cm)を計算して得られたものとする。また、圧縮処理によって得られた複数の第3のカーボンナノファイバー80は、複数の第3のカーボンナノファイバーが寄り集まって板状の塊となった複数の板状の第3のカーボンナノファイバー集合体に造粒されることができる。このように板状の塊になって第3のカーボンナノファイバー80を取り扱うことができるので、保管時、運搬時または配合時における取り扱い性を向上することができる。
First, the step (b) using compression processing will be described.
The 3rd carbon nanofiber obtained by the compression process in a process (b) can have no branch part. The compression treatment in the step (b) requires a high pressure for cutting the second carbon nanofiber from at least the branch portion. Here, step (b) will be described in detail with reference to FIG. FIG. 2 is a perspective view schematically showing the step (b) according to the embodiment of the present invention. As shown in FIG. 2, the compression treatment is performed by introducing the second carbon nanofiber 60 as a raw material between a plurality of, for example, at least two rolls 72 and 74 that continuously rotate in the direction of the arrow in the drawing, For example, a dry compression granulator 70 such as a roll press machine or a roller compactor (roll type high pressure compression molding machine) that performs compression force on the first carbon nanofibers can be employed. A plurality of second carbon nanofibers 60 obtained in the step (a) are put into a dry compression granulator 70 and compressed to obtain an aggregate of a plurality of third carbon nanofibers 80. it can. The roll press machine normally uses a smooth roll that does not engrave pockets on the outer peripheral surface of the roll or a roll that engraves pockets. In this embodiment, the roll press machine is smooth to apply a compressive force evenly to the second carbon nanofibers. A roll can be used. The distance between the two rolls is set to 0 mm, that is, the rolls are in contact with each other, and a predetermined compression force F, for example, 980 to 2940 N / cm can be applied between the two rolls, and further 1500 to 2500 N / Cm is preferred. The compressive force F can be set to an appropriate pressure while confirming the presence or absence of a branched portion in the obtained carbon nanofiber aggregate with an electron microscope or the like. If it is 980 N / cm or more, the 2nd carbon nanofiber which has a branch part can be cut | disconnected by a branch part. Such compression treatment can be performed a plurality of times, for example, about twice in order to homogenize the entire carbon nanofiber. In the granulator, a binder such as water is generally blended to bind powder, but the compression treatment in the present embodiment is a dry granulation that does not use a binder for binding third carbon nanofibers. Can be. This is because if a binder is used, it may be difficult to disperse the fourth carbon nanofibers in a later step, and a step of removing the binder may be further required.
Normally, after compression between two rolls by a dry compression granulator 70 to form an aggregate of plate-like (flakes) carbon nanofibers 80, the powder is further crushed by a pulverizer or the like, An aggregate of carbon nanofibers 80 sized to a size can be produced. The pulverizer at this time, for example, rotates the rotary blade at high speed and crushes the aggregate of carbon nanofibers 80 by the shearing force, and uses a screen to adjust the size only through the aggregate of carbon nanofibers 80 having an appropriate size or less. It can be performed. The size of the aggregates of the carbon nanofibers 80 varies greatly only by the compression treatment, but the particle size of the aggregates of the carbon nanofibers 80 is adjusted to an appropriate size by further crushing in this way, so that the matrix material It is possible to prevent the carbon nanofiber aggregates from being biased when kneaded. By this compression treatment, the third carbon nanofibers are cut at the branching portions, become a desired bulk density that does not fluff and become easy to handle, and are granulated into, for example, a plate-like third carbon nanofiber aggregate. be able to.
The 3rd carbon nanofiber obtained by compressing is demonstrated in detail using FIG. FIG. 3 is a diagram schematically showing a third carbon nanofiber according to an embodiment of the present invention.
As shown in FIG. 3, the second carbon nanofiber 60 having the branch part 64 shown on the upper left side of the figure is cut from the branch part 64 by the compression process, and for example 4 as shown on the lower right side of the figure. A third carbon nanofiber 80 of the book is obtained. Therefore, the third carbon nanofibers 80 can reduce the number of branch portions 64 as compared with the second carbon nanofibers 60. In particular, even when observed with an electron microscope, the branch portions 64 can be eliminated. Thus, the third carbon nanofiber having no branch portion becomes the fourth carbon nanofiber through the step (c), and the fourth carbon nanofiber in the composite material is mixed with other materials. Dispersibility can be improved, and flexibility and durability of the composite material can be improved. Furthermore, since the fourth carbon nanofiber does not have a branching portion, when it is compounded in the composite material, there is no stress concentration on the branching portion of the fourth carbon nanofiber, and as a reinforcing material for the fourth carbon nanofiber. The performance degradation can be reduced. Since a part of the second carbon nanofiber having the bent part 62 as shown in FIG. 1C is also cut from the bent part 62, the second carbon nanofiber having the so-called defective part such as the bent part 62 and the branch part 64. 3 carbon nanofibers can be reduced. Of the third carbon nanofibers 80 obtained by the compression treatment, the ratio of the third carbon nanofibers having the bent portions 62 may be less than 10 out of 100. When the ratio including the third carbon nanofibers having the bent portion 62 is 10 or more out of 100, there is a possibility that the defective portion cannot be sufficiently removed by the compression treatment. Thus, the 3rd carbon nanofiber 80 in which the defect parts like the bending part 62 and the branch part 64 reduced can have a maximum fiber length of less than 20 μm. In recent years, as the market demand, it is sometimes preferred that the maximum fiber length of carbon nanofibers is less than 20 μm, and more preferably less than 15 μm. For example, by setting the maximum fiber length of the third carbon nanofiber to less than 20 μm, the flexibility of the composite material containing the fourth carbon nanofiber can be improved. The plurality of third carbon nanofibers 80 may have a bulk density of 0.15 to 0.3 g / cm 3 . If the bulk density is 0.15 to 0.3 g / cm 3 , the third carbon nanofibers 80 are difficult to scatter and can be easily handled during storage, transportation or compounding, and handling properties are also good. Note that the bulk density in this application is JIS-K6219-2 carbon black for rubber-measurement of granulated particles-part 2 according to the measurement of bulk density, carbon nanofibers are poured into a 1000 cm 3 cylindrical container and the mass is calculated. Measured and obtained by calculating the bulk density (g / cm 3 ). In addition, the plurality of third carbon nanofibers 80 obtained by the compression treatment is a set of a plurality of plate-like third carbon nanofibers in which a plurality of third carbon nanofibers gather to form a plate-like lump. Can be granulated in the body. Thus, since it becomes a plate-shaped lump and the 3rd carbon nanofiber 80 can be handled, the handleability at the time of storage, at the time of conveyance, or a mixing | blending can be improved.

 次に、粉砕処理を用いた工程(b)について説明する。
工程(b)における粉砕処理によって得られた第3のカーボンナノファイバーのタップ密度は、工程(a)で得られた第2のカーボンナノファイバーのタップ密度の1.5倍~10倍であることができる。工程(b)は、第3のカーボンナノファイバーの窒素吸着比表面積を粉砕処理前の第2のカーボンナノファイバーの窒素吸着比表面積の1.1倍~5.0倍とすることができる。工程(b)によれば、マトリックス材料例えばエラストマーとの表面反応性が向上し、マトリックス材料に対する濡れ性が改善されたカーボンナノファイバーを製造することができる。
第2のカーボンナノファイバーは、繊維が分岐した分岐部分や繊維が屈曲した屈曲部分などの欠陥を有しているが、粉砕処理によって分岐部分付近や屈曲部分で破壊されて欠陥が低減すると共に、カーボンナノファイバーの表面も活性化される。この欠陥低減によってカーボンナノファイバーは分岐部分や屈曲部分が減少するため各繊維の強度は向上し、しかも繊維長がほとんど短くならない程度に粉砕処理されるため、このカーボンナノファイバーを用いた複合材料の物性が向上する。また、カーボンナノファイバーの表面が活性化されることで、カーボンナノファイバーとマトリックス材料との表面反応性が向上し、マトリックス材料中におけるカーボンナノファイバーの分散不良を改善することができる。工程(b)は、衝撃及び/または剪断力を利用した乾式粉砕で行なうことができる。乾式粉砕は、例えば、水または/及び有機溶剤の非存在下で行なうことができる。乾式粉砕は、粉砕後の分散剤の除去及び溶媒の乾燥、乾燥凝集した繊維の解繊という後処理工程がなく、有利である。このような乾式粉砕は、周速度が50~200m/sで0.5~60分間行なわれることができる。乾式粉砕としては、高速回転ミル、ボールミル、媒体攪拌ミル、ジェット粉砕機などを用いることができるが、衝撃力を利用した繊維を押し砕く方法による回転式粉砕機、円振動ミル、遠心ミルなどの振動ボールミルを採用することができる。
このように、粉砕処理は、例えば前記圧縮処理と同様に、分岐部を有する第2のカーボンナノファイバーが分岐部から切断され、分岐部を減らすことができる。したがって、粉砕処理された第3のカーボンナノファイバーは、第2のカーボンナノファイバーよりも分岐部を減らすことができ、特に、電子顕微鏡で観察しても分岐部がなくなることができる。
粉砕処理後の第3のカーボンナノファイバーのタップ密度は、粉砕処理前の第2のタップ密度の1.5倍~10倍であることができる。このように適度な粉砕処理を行うことで、第2のカーボンナノファイバーの繊維長をほとんど損なうことなく、マトリックス材料例えばエラストマーとの濡れ性を良好にすることができる。粉砕処理後の第3のカーボンナノファイバーは、タップ密度が0.03~0.2g/cmであることができる。タップ密度は、タップ法により測定された見かけ密度であって、第3のカーボンナノファイバーの嵩度合いを表している。したがって、粉砕処理によって第3のカーボンナノファイバーにおける分岐箇所や欠陥が減少すると、密に詰まり易くなり、タップ密度は増加する傾向がある。前記範囲のタップ密度を有する粉砕処理された第3のカーボンナノファイバーは、マトリックス材料例えばエラストマーとの濡れ性が良好となる傾向がある。
また、粉砕処理後の第3のカーボンナノファイバーの窒素吸着比表面積は、粉砕処理前の第2のカーボンナノファイバーの窒素吸着比表面積の1.1倍~5.0倍であることができる。このように窒素吸着比表面積が増大すると、マトリクス材料と第3のカーボンナノファイバーとの接点が増加することになり、マトリクス材料中で分散し易くなる。粉砕処理後の第3のカーボンナノファイバーは、窒素吸着比表面積が22~100m/gであることが好ましい。前記範囲の窒素吸着比表面積を有する粉砕処理された第3のカーボンナノファイバーは、マトリックス材料例えばエラストマーとの濡れ性が良好となる傾向がある。
Next, the step (b) using the pulverization process will be described.
The tap density of the third carbon nanofibers obtained by the pulverization process in the step (b) is 1.5 to 10 times the tap density of the second carbon nanofibers obtained in the step (a). Can do. In the step (b), the nitrogen adsorption specific surface area of the third carbon nanofiber can be 1.1 to 5.0 times the nitrogen adsorption specific surface area of the second carbon nanofiber before pulverization. According to the step (b), carbon nanofibers having improved surface reactivity with a matrix material such as an elastomer and improved wettability to the matrix material can be produced.
The second carbon nanofiber has defects such as a branched portion where the fiber is branched and a bent portion where the fiber is bent. The surface of the carbon nanofiber is also activated. By reducing the defects, the carbon nanofibers are reduced in branching and bending portions, so that the strength of each fiber is improved and the fiber length is pulverized to such an extent that the fiber length is hardly reduced. Physical properties are improved. In addition, by activating the surface of the carbon nanofibers, the surface reactivity between the carbon nanofibers and the matrix material is improved, and poor dispersion of the carbon nanofibers in the matrix material can be improved. Step (b) can be performed by dry grinding using impact and / or shearing force. The dry pulverization can be performed in the absence of water or / and an organic solvent, for example. Dry pulverization is advantageous because there are no post-treatment steps such as removal of the dispersant after pulverization, drying of the solvent, and defibration of the dried and agglomerated fibers. Such dry pulverization can be performed at a peripheral speed of 50 to 200 m / s for 0.5 to 60 minutes. As the dry pulverization, a high-speed rotary mill, a ball mill, a medium stirring mill, a jet pulverizer, or the like can be used. A vibrating ball mill can be employed.
As described above, in the pulverization process, for example, the second carbon nanofibers having the branch part are cut from the branch part, and the branch parts can be reduced, similarly to the compression process. Therefore, the pulverized third carbon nanofibers can have fewer branch portions than the second carbon nanofibers, and in particular, the branch portions can be eliminated even when observed with an electron microscope.
The tap density of the third carbon nanofibers after the pulverization process can be 1.5 to 10 times the second tap density before the pulverization process. By performing an appropriate pulverization treatment in this manner, wettability with a matrix material such as an elastomer can be improved without substantially impairing the fiber length of the second carbon nanofibers. The third carbon nanofibers after the pulverization treatment can have a tap density of 0.03 to 0.2 g / cm 3 . The tap density is an apparent density measured by the tap method, and represents the degree of bulk of the third carbon nanofiber. Therefore, if the branching locations and defects in the third carbon nanofibers are reduced by the pulverization process, the third carbon nanofibers tend to be densely packed and the tap density tends to increase. The pulverized third carbon nanofibers having a tap density in the above range tend to have good wettability with a matrix material such as an elastomer.
Further, the nitrogen adsorption specific surface area of the third carbon nanofibers after the pulverization treatment can be 1.1 to 5.0 times the nitrogen adsorption specific surface area of the second carbon nanofibers before the pulverization treatment. When the nitrogen adsorption specific surface area increases in this way, the number of contacts between the matrix material and the third carbon nanofibers increases, which facilitates dispersion in the matrix material. The third carbon nanofiber after the pulverization treatment preferably has a nitrogen adsorption specific surface area of 22 to 100 m 2 / g. The pulverized third carbon nanofiber having a nitrogen adsorption specific surface area in the above range tends to have good wettability with a matrix material such as an elastomer.

 最後に、工程(c)として、前記工程(b)で得られた第3のカーボンナノファイバーを酸素を含有する雰囲気中で600℃~800℃で熱処理して、酸化した第4のカーボンナノファイバーを得ることができる。
工程(c)は、例えば、大気雰囲気の炉内に第3のカーボンナノファイバーを配置し、600℃~800℃の温度範囲の所定温度に設定し、熱処理することによって、表面が所望の酸素濃度に酸化された第4のカーボンナノファイバーを得ることができる。この工程(c)で熱処理する時間は、所定温度の熱処理炉内で第3のカーボンナノファイバーを保持する時間であって、例えば10分~180分であることができる。酸素を含有する雰囲気は、大気中でもよいし、酸素雰囲気でもよいし、適宜酸素濃度を設定した雰囲気を用いてもよいが、熱処理炉の内容量や処理する第3のカーボンナノファイバーの量によって熱処理炉に導入する酸素の量を適宜調節することができる。第4のカーボンナノファイバーの表面が工程(c)で所望の酸素濃度に酸化されるのに十分な酸素濃度が雰囲気中に存在すればよい。熱処理の温度は、600℃~800℃の範囲で所望の酸化処理を得るために適宜設定することができる。通常、800℃付近で第3のカーボンナノファイバーは燃焼して繊維に大きなダメージを負うため、温度設定と熱処理の時間は実験を繰り返しながら慎重に設定することが望ましい。なお、熱処理の温度や熱処理の時間は、工程(c)に用いる炉内の酸素濃度や炉の内容積、処理する第3のカーボンナノファイバーの量などによって適宜調整することができる。また、本実施の形態における熱処理温度とは、熱処理炉内の雰囲気温度を示す。
工程(c)は、X線光電子分光法(XPS)で測定した、第3のカーボンナノファイバーの表面の酸素濃度に対する第4のカーボンナノファイバーの表面の酸素濃度の増加量が、0.5atm%~2.6atm%になるように酸化処理を行うことができる。このような第3のカーボンナノファイバーの表面酸素濃度に対する第4のカーボンナノファイバーの表面酸素濃度の増加量は、工程(b)における機械的作用による処理を圧縮処理によって行った場合は0.9atm%~2.6atm%であることができ、さらに1.0atm%~2.6atm%であることができ、工程(b)における機械的作用による処理を粉砕処理によって行った場合は0.9atm%~1.9atm%であることができ、さらに1.0atm%~1.6atm%であることができる。また、工程(c)は、X線光電子分光法(XPS)で測定した、第3のカーボンナノファイバーの表面の酸素濃度に対する第4のカーボンナノファイバーの表面の酸素濃度の増加割合が、20%~120%になるように酸化処理を行うことができる。このような第3のカーボンナノファイバーの表面酸素濃度に対する第4のカーボンナノファイバーの表面酸素濃度の増加割合は、工程(b)における機械的作用による処理を圧縮処理によって行った場合は60%~120%であることができ、工程(b)における機械的作用による処理を粉砕処理によって行った場合は43%~90%であることができ、さらに48%~76%であることができる。工程(c)で得られた第4のカーボンナノファイバーのX線光電子分光法(XPS)で測定した表面の酸素濃度は、2.6atm%~4.6atm%であることができ、工程(b)における機械的作用による処理を圧縮処理によって行った場合は3.0atm%~4.6atm%であることができ、さらに3.1atm%~4.6atm%であることができ、工程(b)における機械的作用による処理を粉砕処理によって行った場合は3.0atm%~4.0atm%であることができ、さらに3.1atm%~3.7atm%であることができる。このように、第3のカーボンナノファイバーの表面が適度に酸化していることで、第4のカーボンナノファイバーとエラストマーとの表面反応性が向上し、エラストマー中におけるカーボンナノファイバーの分散不良を改善することができる。
このように工程(c)で酸化処理された第4のカーボンナノファイバーの質量は、第3のカーボンナノファイバーの質量より例えば2%~20%減量することができ、この減量の範囲であれば第4のカーボンナノファイバーが適度に酸化していると推測できる。第4のカーボンナノファイバーの質量が第3のカーボンナノファイバーの質量より2%未満しか減量していないと、第4のカーボンナノファイバーの表面の酸素濃度が低いため濡れ性の向上が得にくい傾向がある。また、第3のカーボンナノファイバーの質量より20%を超えて減量した第4のカーボンナノファイバーは、減量が20%以下の第4のカーボンナノファイバーに比べて濡れ性がほとんど変わらないにもかかわらず、酸化処理によるカーボンナノファイバーの減量による損失が大きく、しかも熱処理のエネルギー消費量に対して経済的にも不利になる傾向がある。第3のカーボンナノファイバーの表面が酸化することによって、第3のカーボンナノファイバーの表面の炭素の一部が炭酸ガスとして気化して減量することになるからである。第4のカーボンナノファイバーの質量が第3のカーボンナノファイバーの質量より20%を超えなければ繊維長がほとんど短くならないと推測できるため好ましい。なお、第4のカーボンナノファイバーの表面の酸素濃度は、XPS(X線光電子分光法)によって分析することができる。XPSによる酸素濃度の分析は、第4のカーボンナノファイバーの表面に付着した不純物を除去するために、測定前の第4のカーボンナノファイバーに対し例えば0.5分~1.0分間のアルゴンガスエッチングを行い、第4のカーボンナノファイバーの清浄な表面を出してから分析を行うことが好ましい。このアルゴンガスエッチングのアルゴンガス濃度は、5×10−2Pa~20×10−2Paであることができる。また、XPSによる酸素濃度の分析は、XPS装置の金属台の上に導電性接着剤である例えばカーボンテープを貼り、そのカーボンテープ上に第4のカーボンナノファイバーをふりかけてカーボンテープに付着させ、カーボンテープに付着しなかった余分な第4のカーボンナノファイバーを振り落として取り除いた状態で行うことができる。このように、XPSによる酸素濃度の分析においては、第4のカーボンナノファイバーをカーボンテープ上に押しつけてブロック状に固めることなく、なるべく粉体に近い状態で分析することができる。なお、第3のカーボンナノファイバーも同様にXPS装置で測定することができる。
Finally, as the step (c), the third carbon nanofiber obtained in the step (b) is heat-treated at 600 ° C. to 800 ° C. in an oxygen-containing atmosphere to oxidize the fourth carbon nanofiber. Can be obtained.
In step (c), for example, the third carbon nanofiber is placed in a furnace in an air atmosphere, set to a predetermined temperature in the temperature range of 600 ° C. to 800 ° C., and heat-treated, so that the surface has a desired oxygen concentration. A fourth carbon nanofiber oxidized to can be obtained. The heat treatment time in this step (c) is the time for holding the third carbon nanofibers in a heat treatment furnace at a predetermined temperature, and can be, for example, 10 minutes to 180 minutes. The atmosphere containing oxygen may be air, an oxygen atmosphere, or an atmosphere in which an oxygen concentration is appropriately set. However, heat treatment is performed depending on the content of the heat treatment furnace and the amount of the third carbon nanofiber to be treated. The amount of oxygen introduced into the furnace can be adjusted as appropriate. A sufficient oxygen concentration may be present in the atmosphere so that the surface of the fourth carbon nanofiber is oxidized to the desired oxygen concentration in the step (c). The temperature of the heat treatment can be appropriately set in order to obtain a desired oxidation treatment in the range of 600 ° C to 800 ° C. Usually, since the third carbon nanofibers burn and cause great damage to the fibers at around 800 ° C., it is desirable to set the temperature setting and the heat treatment time carefully while repeating the experiment. The heat treatment temperature and heat treatment time can be appropriately adjusted depending on the oxygen concentration in the furnace used in the step (c), the inner volume of the furnace, the amount of the third carbon nanofiber to be treated, and the like. In addition, the heat treatment temperature in the present embodiment indicates the atmospheric temperature in the heat treatment furnace.
In the step (c), the increase in the oxygen concentration on the surface of the fourth carbon nanofiber relative to the oxygen concentration on the surface of the third carbon nanofiber measured by X-ray photoelectron spectroscopy (XPS) is 0.5 atm%. The oxidation treatment can be performed so as to be ~ 2.6 atm%. The amount of increase in the surface oxygen concentration of the fourth carbon nanofiber relative to the surface oxygen concentration of the third carbon nanofiber is 0.9 atm when the mechanical action in the step (b) is performed by the compression treatment. % To 2.6 atm%, and further 1.0 to 2.6 atm%, and 0.9 atm% when the mechanical action in the step (b) is performed by pulverization. It can be ˜1.9 atm%, and further can be 1.0 atm% to 1.6 atm%. In the step (c), the rate of increase in the oxygen concentration on the surface of the fourth carbon nanofiber relative to the oxygen concentration on the surface of the third carbon nanofiber measured by X-ray photoelectron spectroscopy (XPS) is 20%. Oxidation treatment can be performed so as to be ~ 120%. The increase ratio of the surface oxygen concentration of the fourth carbon nanofiber to the surface oxygen concentration of the third carbon nanofiber is 60% when the treatment by the mechanical action in the step (b) is performed by the compression treatment. 120%, and when the mechanical action in the step (b) is performed by pulverization, it can be 43% to 90%, and further can be 48% to 76%. The surface oxygen concentration measured by X-ray photoelectron spectroscopy (XPS) of the fourth carbon nanofiber obtained in the step (c) can be 2.6 atm% to 4.6 atm%, and the step (b ) In the case where the processing by the mechanical action is performed by the compression treatment, it can be 3.0 atm% to 4.6 atm%, and further can be 3.1 atm% to 4.6 atm%, step (b) In the case where the treatment by the mechanical action is performed by pulverization treatment, it can be 3.0 atm% to 4.0 atm%, and further can be 3.1 atm% to 3.7 atm%. As described above, the surface of the third carbon nanofiber is appropriately oxidized to improve the surface reactivity between the fourth carbon nanofiber and the elastomer, thereby improving the dispersion of the carbon nanofiber in the elastomer. can do.
Thus, the mass of the fourth carbon nanofibers oxidized in the step (c) can be reduced by 2% to 20%, for example, from the mass of the third carbon nanofibers. It can be estimated that the fourth carbon nanofibers are appropriately oxidized. If the mass of the fourth carbon nanofiber is less than 2% less than the mass of the third carbon nanofiber, the oxygen concentration on the surface of the fourth carbon nanofiber is low, and it is difficult to improve the wettability. There is. Moreover, although the 4th carbon nanofiber reduced in weight by more than 20% than the mass of the 3rd carbon nanofiber has a wettability almost the same as that of the 4th carbon nanofiber whose weight loss is 20% or less. However, the loss due to the reduction of the carbon nanofibers due to the oxidation treatment is large, and it tends to be economically disadvantageous for the energy consumption of the heat treatment. This is because, when the surface of the third carbon nanofiber is oxidized, a part of the carbon on the surface of the third carbon nanofiber is vaporized as carbon dioxide gas to be reduced. It is preferable because it can be estimated that the length of the fourth carbon nanofiber does not become almost shorter unless the mass of the fourth carbon nanofiber exceeds 20% of the mass of the third carbon nanofiber. The oxygen concentration on the surface of the fourth carbon nanofiber can be analyzed by XPS (X-ray photoelectron spectroscopy). The analysis of the oxygen concentration by XPS is performed by, for example, argon gas for 0.5 minute to 1.0 minute with respect to the fourth carbon nanofiber before measurement in order to remove impurities attached to the surface of the fourth carbon nanofiber. It is preferable to perform analysis after etching to bring out the clean surface of the fourth carbon nanofiber. The argon gas concentration of the argon gas etching can be 5 × 10 −2 Pa to 20 × 10 −2 Pa. In addition, the analysis of the oxygen concentration by XPS is performed by attaching a carbon tape that is a conductive adhesive on a metal base of the XPS device, and then spraying the fourth carbon nanofiber on the carbon tape to adhere to the carbon tape, It can be performed in a state in which excess fourth carbon nanofibers not attached to the carbon tape are shaken off. As described above, in the analysis of the oxygen concentration by XPS, the analysis can be performed in a state as close to powder as possible without pressing the fourth carbon nanofibers on the carbon tape and solidifying the block. Similarly, the third carbon nanofiber can be measured with an XPS apparatus.

 工程(c)によって得られた第4のカーボンナノファイバーは、ラマン散乱分光法によって測定される1600cm−1付近のピーク強度Gに対する1300cm−1付近のピーク強度Dの比(D/G)が0.12~0.22であることができる。第4のカーボンナノファイバーのラマンピーク比(D/G)は、その表面の結晶に欠陥が多くなるため、第3のカーボンナノファイバーのラマンピーク比(D/G)よりも大きくなる。第4のカーボンナノファイバーは、そのラマンピーク比(D/G)が第3のカーボンナノファイバーのラマンピーク比(D/G)より0.02以上増加する程度に酸化することが望ましい。また、第4のカーボンナノファイバーは、窒素吸着比表面積が34m/g~58m/gであることができる。第4のカーボンナノファイバーの窒素吸着比表面積は、その表面が荒れるため、第3のカーボンナノファイバーの窒素吸着比表面積よりも大きくなる。第4のカーボンナノファイバーは、その窒素吸着比表面積が第3のカーボンナノファイバーの窒素吸着比表面積より9m/g以上増加する程度に酸化することが望ましい。工程(c)に用いられる第4のカーボンナノファイバーの平均直径は第1のカーボンナノファイバーの平均直径とほとんど変わらない。このような気相成長法で得られた第4のカーボンナノファイバーの平均直径は、70nm~100nmであることができる。このような第4のカーボンナノファイバーを用いることにより、エラストマーとの表面反応性が向上し、エラストマーに対する濡れ性を改善することができ、体積固有抵抗値が高く電気絶縁性能に優れた炭素繊維複合材料を得ることができる。第4のカーボンナノファイバーのエラストマーへの配合量は、用途に応じて設定することができるが、第4のカーボンナノファイバーはエラストマーとの濡れ性が向上しているため、例えば同じ剛性の炭素繊維複合材料を製造する場合、従来よりも配合量を減らすことができる。 Fourth carbon nanofibers obtained by the step (c), the ratio of the peak intensity D of around 1300 cm -1 to the peak intensity G of around 1600 cm -1 measured by Raman scattering spectroscopy (D / G) is 0 .12 to 0.22. The Raman peak ratio (D / G) of the fourth carbon nanofiber is larger than the Raman peak ratio (D / G) of the third carbon nanofiber because the crystal on the surface has many defects. The fourth carbon nanofiber is desirably oxidized to such an extent that its Raman peak ratio (D / G) increases by 0.02 or more than the Raman peak ratio (D / G) of the third carbon nanofiber. The fourth carbon nanofiber may have a nitrogen adsorption specific surface area of 34 m 2 / g to 58 m 2 / g. The nitrogen adsorption specific surface area of the fourth carbon nanofiber is larger than the nitrogen adsorption specific surface area of the third carbon nanofiber because the surface thereof is rough. The fourth carbon nanofiber is desirably oxidized to such an extent that its nitrogen adsorption specific surface area is increased by 9 m 2 / g or more from the nitrogen adsorption specific surface area of the third carbon nanofiber. The average diameter of the fourth carbon nanofibers used in the step (c) is almost the same as the average diameter of the first carbon nanofibers. The average diameter of the fourth carbon nanofibers obtained by such a vapor phase growth method can be 70 nm to 100 nm. By using such a fourth carbon nanofiber, the surface reactivity with the elastomer is improved, the wettability to the elastomer can be improved, and the carbon fiber composite having a high volume resistivity and excellent electrical insulation performance. Material can be obtained. The blending amount of the fourth carbon nanofibers into the elastomer can be set according to the use. However, since the fourth carbon nanofibers have improved wettability with the elastomer, for example, carbon fibers having the same rigidity are used. When manufacturing a composite material, a compounding quantity can be reduced conventionally.

 (II)エラストマー
次に、炭素繊維複合材料の製造方法に用いられるエラストマーについて説明する。
エラストマーは、重量平均分子量が5000~500万であることができ、さらに2万~300万であることができる。エラストマーの分子量がこの範囲であると、エラストマー分子が互いに絡み合い、相互につながっているので、エラストマーは、第4のカーボンナノファイバーを分散させるために良好な弾性を有している。エラストマーは、粘性を有しているので凝集した第4のカーボンナノファイバーの相互に侵入しやすく、さらに弾性を有することによって第4のカーボンナノファイバー同士を分離することができるため好ましい。エラストマーは、パルス法NMRを用いてハーンエコー法によって、30℃、観測核がHで測定した、未架橋体におけるネットワーク成分のスピン−スピン緩和時間(T2n/30℃)が100~3000μ秒であることができ、さらに200~1000μ秒であることができる。上記範囲のスピン−スピン緩和時間(T2n/30℃)を有することにより、エラストマーは、柔軟で充分に高い分子運動性を有することができ、すなわち第4のカーボンナノファイバーを分散させるために適度な弾性を有することができる。また、エラストマーは粘性を有しているので、エラストマーと第4のカーボンナノファイバーとを混合したときに、エラストマーは高い分子運動により第4のカーボンナノファイバーの相互の隙間に容易に侵入することができる。また、エラストマーは、パルス法NMRを用いてハーンエコー法によって30℃、観測核がHで測定した、架橋体における、ネットワーク成分のスピン−スピン緩和時間(T2n)が100~2000μ秒であることができる。その理由は、上述した未架橋体と同様である。すなわち、上記の条件を有する未架橋体を架橋化すると、得られる架橋体のT2nはおおよそ上記範囲に含まれることができる。
(II) Elastomer Next, the elastomer used in the method for producing the carbon fiber composite material will be described.
The elastomer may have a weight average molecular weight of 5,000 to 5,000,000, and further 20,000 to 3,000,000. When the molecular weight of the elastomer is within this range, the elastomer molecules are entangled with each other and are connected to each other. Therefore, the elastomer has good elasticity for dispersing the fourth carbon nanofibers. The elastomer is preferable because it has a viscosity, so that the agglomerated fourth carbon nanofibers can easily enter each other, and the fourth carbon nanofibers can be separated from each other by having elasticity. The elastomer has a spin-spin relaxation time (T2n / 30 ° C.) of the network component in the uncrosslinked body of 100 to 3000 μsec, measured at 30 ° C. by the Hahn echo method using pulsed NMR, and the observation nucleus is 1 H. Can be 200-1000 μs. By having a spin-spin relaxation time (T2n / 30 ° C.) in the above range, the elastomer can be flexible and have sufficiently high molecular mobility, that is, suitable for dispersing the fourth carbon nanofibers. It can have elasticity. In addition, since the elastomer has viscosity, when the elastomer and the fourth carbon nanofiber are mixed, the elastomer can easily enter the gap between the fourth carbon nanofibers due to high molecular motion. it can. The elastomer has a network component spin-spin relaxation time (T2n) of 100 to 2000 μsec measured at 30 ° C. by the Hahn-echo method using pulsed NMR and the observation nucleus at 1 H. Can do. The reason is the same as that of the uncrosslinked product described above. That is, when an uncrosslinked body having the above conditions is crosslinked, T2n of the obtained crosslinked body can be approximately included in the above range.

 パルス法NMRを用いたハーンエコー法によって得られるスピン−スピン緩和時間は、物質の分子運動性を表す尺度である。具体的には、パルス法NMRを用いたハーンエコー法によりエラストマーのスピン−スピン緩和時間を測定すると、緩和時間の短い第1のスピン−スピン緩和時間(T2n)を有する第1の成分と、緩和時間のより長い第2のスピン−スピン緩和時間(T2nn)を有する第2の成分とが検出される。第1の成分は高分子のネットワーク成分(骨格分子)に相当し、第2の成分は高分子の非ネットワーク成分(末端鎖などの枝葉の成分)に相当する。そして、第1のスピン−スピン緩和時間が短いほど分子運動性が低く、エラストマーは固いといえる。また、第1のスピン−スピン緩和時間が長いほど分子運動性が高く、エラストマーは柔らかいといえる。パルス法NMRにおける測定法としては、ハーンエコー法でなくてもソリッドエコー法、CPMG法(カー・パーセル・メイブーム・ギル法)あるいは90°パルス法でも適用できる。ただし、本発明にかかるエラストマーは中程度のスピン−スピン緩和時間(T2)を有するので、ハーンエコー法が最も適している。一般的に、ソリッドエコー法および90°パルス法は、短いT2の測定に適し、ハーンエコー法は、中程度のT2の測定に適し、CPMG法は、長いT2の測定に適している。 The spin-spin relaxation time obtained by the Hahn-echo method using pulsed NMR is a measure representing the molecular mobility of a substance. Specifically, when the spin-spin relaxation time of the elastomer is measured by the Hahn-echo method using pulsed NMR, a first component having a first spin-spin relaxation time (T2n) having a short relaxation time, and relaxation A second component having a longer spin-spin relaxation time (T2nn) is detected. The first component corresponds to a polymer network component (skeleton molecule), and the second component corresponds to a polymer non-network component (branch and leaf component such as a terminal chain). The shorter the first spin-spin relaxation time, the lower the molecular mobility and the harder the elastomer. Further, it can be said that the longer the first spin-spin relaxation time, the higher the molecular mobility and the softer the elastomer. As a measurement method in the pulse method NMR, the solid echo method, the CPMG method (Car Purcell, Mayboom, Gill method) or the 90 ° pulse method can be applied even if it is not the Hahn echo method. However, since the elastomer according to the present invention has a medium spin-spin relaxation time (T2), the Hahn echo method is most suitable. In general, the solid echo method and the 90 ° pulse method are suitable for short T2 measurement, the Hahn echo method is suitable for medium T2 measurement, and the CPMG method is suitable for long T2 measurement.

 エラストマーは、主鎖、側鎖および末端鎖の少なくともひとつに、カーボンナノファイバーの末端のラジカルに対して親和性を有する不飽和結合または基を有するか、もしくは、このようなラジカルまたは基を生成しやすい性質を有する。かかる不飽和結合または基としては、例えば、二重結合、三重結合、カルボニル基、カルボキシル基、水酸基、アミノ基、ニトリル基、ケトン基、アミド基、エポキシ基、エステル基、ビニル基、ハロゲン基、ウレタン基、ビューレット基、アロファネート基および尿素基などの官能基から選択される少なくともひとつであることができる。本実施の形態では、エラストマーの主鎖、側鎖および末端鎖の少なくともひとつに、カーボンナノファイバーのラジカルと親和性(反応性または極性)が高い不飽和結合や基を有することにより、エラストマーと第4のカーボンナノファイバーとを結合することができる。このことにより、第4のカーボンナノファイバーの凝集力にうち勝ってその分散を容易にすることができる。そして、エラストマーと、第4のカーボンナノファイバーと、を混練する際に、エラストマーの分子鎖が切断されて生成したフリーラジカルは、第4のカーボンナノファイバーの欠陥を攻撃し、第4のカーボンナノファイバーの表面にラジカルを生成すると推測できる。 The elastomer has an unsaturated bond or group having affinity for the radical at the end of the carbon nanofiber in at least one of the main chain, the side chain and the end chain, or generates such a radical or group. Easy to use. Examples of such unsaturated bonds or groups include double bonds, triple bonds, carbonyl groups, carboxyl groups, hydroxyl groups, amino groups, nitrile groups, ketone groups, amide groups, epoxy groups, ester groups, vinyl groups, halogen groups, It can be at least one selected from functional groups such as urethane groups, burette groups, allophanate groups and urea groups. In this embodiment, at least one of the main chain, side chain, and terminal chain of the elastomer has an unsaturated bond or group having high affinity (reactivity or polarity) with the radical of the carbon nanofiber, so that 4 carbon nanofibers can be bonded. Thereby, it is possible to easily disperse the fourth carbon nanofiber by overcoming the cohesive force. Then, when the elastomer and the fourth carbon nanofiber are kneaded, the free radical generated by breaking the molecular chain of the elastomer attacks the defect of the fourth carbon nanofiber, and the fourth carbon nanofiber is attacked. It can be assumed that radicals are generated on the surface of the fiber.

 エラストマーとしては、天然ゴム(NR)、エポキシ化天然ゴム(ENR)、スチレン−ブタジエンゴム(SBR)、ニトリルゴム(NBR)、クロロプレンゴム(CR)、エチレン−プロピレンゴム(EPR,EPDM)、ブチルゴム(IIR)、クロロブチルゴム(CIIR)、アクリルゴム(ACM)、シリコーンゴム(Q)、フッ素ゴム(FKM)、パーフロロエラストマー(FFKM)、ブタジエンゴム(BR)、エポキシ化ブタジエンゴム(EBR)、エピクロルヒドリンゴム(CO,CEO)、ウレタンゴム(U)、ポリスルフィドゴム(T)などのエラストマー類;オレフィン系(TPO)、ポリ塩化ビニル系(TPVC)、ポリエステル系(TPEE)、ポリウレタン系(TPU)、ポリアミド系(TPEA)、スチレン系(SBS)、などの熱可塑性エラストマー;およびこれらの混合物を用いることができる。特に、エラストマーの混練の際にフリーラジカルを生成しやすい極性の高いエラストマー、例えば、天然ゴム(NR)、ニトリルゴム(NBR)などが好ましい。また、極性の低いエラストマー、例えばエチレンプロピレンゴム(EPDM)であっても、混練の温度を比較的高温(例えばEPDMの場合、50℃~150℃)とすることで、フリーラジカルを生成するので本発明に用いることができる。なお、フッ素ゴムに代表される含フッ素エラストマーを用いることで第4のカーボンナノファイバーを配合することで、比較的高い体積固有抵抗値を有する炭素繊維複合材料を得ることができる。また、エラストマーは、ゴム系エラストマーあるいは熱可塑性エラストマーのいずれであってもよい。また、ゴム系エラストマーの場合、エラストマーは架橋体あるいは未架橋体のいずれであってもよいが、未架橋体を用いることが好ましい。 As the elastomer, natural rubber (NR), epoxidized natural rubber (ENR), styrene-butadiene rubber (SBR), nitrile rubber (NBR), chloroprene rubber (CR), ethylene-propylene rubber (EPR, EPDM), butyl rubber ( IIR), chlorobutyl rubber (CIIR), acrylic rubber (ACM), silicone rubber (Q), fluorine rubber (FKM), perfluoroelastomer (FFKM), butadiene rubber (BR), epoxidized butadiene rubber (EBR), epichlorohydrin rubber Elastomers such as (CO, CEO), urethane rubber (U), polysulfide rubber (T); olefin (TPO), polyvinyl chloride (TPVC), polyester (TPEE), polyurethane (TPU), polyamide (TPEA), Still System (SBS), thermoplastic elastomers, and the like; and may be a mixture thereof. Particularly preferred are highly polar elastomers that easily generate free radicals during elastomer kneading, such as natural rubber (NR) and nitrile rubber (NBR). Even in the case of an elastomer having a low polarity, such as ethylene propylene rubber (EPDM), free radicals are generated by setting the kneading temperature at a relatively high temperature (for example, 50 ° C. to 150 ° C. in the case of EPDM). Can be used for invention. In addition, the carbon fiber composite material which has a comparatively high volume specific resistance value can be obtained by mix | blending a 4th carbon nanofiber by using the fluorine-containing elastomer represented by fluororubber. The elastomer may be either a rubber-based elastomer or a thermoplastic elastomer. In the case of a rubber-based elastomer, the elastomer may be either a crosslinked body or an uncrosslinked body.

 (III)炭素繊維複合材料の製造方法
本発明の一実施の形態にかかる炭素繊維複合材料の製造方法は、気相成長法によって製造された第1のカーボンナノファイバーを、前記気相成長法における反応温度より高温であって、かつ、1100℃~1600℃で熱処理して第2のカーボンナノファイバーを得る工程(a)と、前記第2のカーボンナノファイバーを機械的作用によって処理して、第2のカーボンナノファイバーの分岐部を減らして、第3のカーボンナノファイバーを得る工程(b)と、前記第3のカーボンナノファイバーを酸素を含有する雰囲気中で600℃~800℃で熱処理して、酸化した第4のカーボンナノファイバーを得る工程(c)と、前記第4のカーボンナノファイバーを、エラストマーに混合し、剪断力で該エラストマー中に均一に分散して炭素繊維複合材料を得る工程(d)と、を含む。工程(a)~(c)については、前記(I)において説明したので省略する。工程(d)について図4~図6を用いて詳細に説明する。
図4~図6は、本発明の一実施形態にかかるオープンロール法による工程(d)を模式的に示す図である。図4~図6に示すように、2本ロールのオープンロール2における第1のロール10と第2のロール20とは、所定の間隔d、例えば0.5mm~1.5mmの間隔で配置され、図4~図6において矢印で示す方向に回転速度V1,V2で正転あるいは逆転で回転する。
まず、図4に示すように、第1のロール10に巻き付けられたエラストマー30の素練りを行ない、エラストマー分子鎖を適度に切断してフリーラジカルを生成する。素練りによって生成されたエラストマーのフリーラジカルが工程(c)で得られた第4のカーボンナノファイバーと結びつきやすい状態となる。
次に、図5に示すように、第1のロール10に巻き付けられたエラストマー30のバンク34に、第4のカーボンナノファイバー90を投入し、混練する。エラストマー30と第4のカーボンナノファイバー90とを混合する工程は、オープンロール法に限定されず、例えば密閉式混練法あるいは多軸押出し混練法を用いることもできる。
さらに、図6に示すように、第1のロール10と第2のロール20とのロール間隔dを、0.5mm以下とすることができ、より好ましくは0~0.5mmの間隔に設定し、混合物36をオープンロール2に投入して薄通しを1回~複数回行なう。薄通しの回数は、例えば1回~10回程度行なうことができる。第1のロール10の表面速度をV1、第2のロール20の表面速度をV2とすると、薄通しにおける両者の表面速度比(V1/V2)は、1.05~3.00であることができ、さらに1.05~1.2であることができる。このような表面速度比を用いることにより、所望の剪断力を得ることができる。このように狭いロール間から押し出された炭素繊維複合材料50は、エラストマー30の弾性による復元力で図6のように大きく変形し、その際にエラストマー30と共に第4のカーボンナノファイバー90が大きく移動する。薄通しして得られた炭素繊維複合材料50は、ロールで圧延されて所定厚さのシート状に分出しされる。この薄通しの工程では、できるだけ高い剪断力を得るために、ロール温度を例えば0~50℃とすることができ、より好ましくは5~30℃の比較的低い温度に設定して行われ、エラストマー30の実測温度も0~50℃に調整することができる。このようにして得られた剪断力により、エラストマー30に高い剪断力が作用し、凝集していた第4のカーボンナノファイバー90がエラストマー分子に1本ずつ引き抜かれるように相互に分離し、エラストマー30中に分散される。特に、エラストマー30は、弾性と、粘性と、第4のカーボンナノファイバー90との化学的相互作用と、を有するため、第4のカーボンナノファイバー90を容易に分散することができる。そして、第4のカーボンナノファイバー90の分散性および分散安定性(第4のカーボンナノファイバーが再凝集しにくいこと)に優れた炭素繊維複合材料50を得ることができる。
(III) Method for Producing Carbon Fiber Composite Material A method for producing a carbon fiber composite material according to an embodiment of the present invention includes the first carbon nanofibers produced by the vapor deposition method in the vapor deposition method. A step (a) of obtaining a second carbon nanofiber by heat treatment at a temperature higher than the reaction temperature and at 1100 ° C. to 1600 ° C., and treating the second carbon nanofiber by mechanical action; The step (b) of obtaining the third carbon nanofiber by reducing the number of branches of the carbon nanofiber 2 and heat-treating the third carbon nanofiber at 600 ° C. to 800 ° C. in an oxygen-containing atmosphere A step (c) of obtaining oxidized fourth carbon nanofibers, and the fourth carbon nanofibers are mixed with an elastomer, and the elastomer is applied with a shearing force. Including the step of obtaining the carbon fiber composite material is uniformly dispersed in the mer (d), the. Steps (a) to (c) have been described in the above (I), and will be omitted. Step (d) will be described in detail with reference to FIGS.
4 to 6 are diagrams schematically showing the step (d) by the open roll method according to the embodiment of the present invention. As shown in FIGS. 4 to 6, the first roll 10 and the second roll 20 in the two-roll open roll 2 are arranged at a predetermined interval d, for example, 0.5 mm to 1.5 mm. 4 to 6, the motor rotates in the direction indicated by the arrow at the rotational speeds V1 and V2 in the normal rotation or reverse rotation.
First, as shown in FIG. 4, the elastomer 30 wound around the first roll 10 is masticated, and the elastomer molecular chain is appropriately cut to generate free radicals. The free radicals of the elastomer generated by mastication are easily combined with the fourth carbon nanofibers obtained in the step (c).
Next, as shown in FIG. 5, the fourth carbon nanofibers 90 are put into the bank 34 of the elastomer 30 wound around the first roll 10 and kneaded. The step of mixing the elastomer 30 and the fourth carbon nanofiber 90 is not limited to the open roll method, and for example, a closed kneading method or a multi-screw extrusion kneading method can also be used.
Further, as shown in FIG. 6, the roll interval d between the first roll 10 and the second roll 20 can be set to 0.5 mm or less, more preferably set to an interval of 0 to 0.5 mm. Then, the mixture 36 is put into the open roll 2 and thinning is performed once to several times. For example, the thinning can be performed about 1 to 10 times. When the surface speed of the first roll 10 is V1 and the surface speed of the second roll 20 is V2, the ratio of the surface speeds (V1 / V2) in thinness is 1.05 to 3.00. Further, it can be 1.05 to 1.2. By using such a surface velocity ratio, a desired shear force can be obtained. The carbon fiber composite material 50 extruded from between the narrow rolls as described above is greatly deformed as shown in FIG. 6 by the restoring force due to the elasticity of the elastomer 30, and the fourth carbon nanofiber 90 moves greatly together with the elastomer 30 at that time. To do. The carbon fiber composite material 50 obtained through thinning is rolled with a roll and dispensed into a sheet having a predetermined thickness. In this thinning process, in order to obtain as high a shearing force as possible, the roll temperature can be set to, for example, 0 to 50 ° C., and more preferably set to a relatively low temperature of 5 to 30 ° C. The actually measured temperature of 30 can also be adjusted to 0 to 50 ° C. Due to the shearing force thus obtained, a high shearing force acts on the elastomer 30, and the aggregated fourth carbon nanofibers 90 are separated from each other so as to be pulled out one by one to the elastomer molecule. Distributed in. In particular, since the elastomer 30 has elasticity, viscosity, and chemical interaction with the fourth carbon nanofibers 90, the fourth carbon nanofibers 90 can be easily dispersed. And the carbon fiber composite material 50 excellent in the dispersibility and dispersion stability of the 4th carbon nanofiber 90 (it is hard to re-aggregate the 4th carbon nanofiber) can be obtained.

 より具体的には、オープンロールでエラストマーと第4のカーボンナノファイバーとを混合すると、粘性を有するエラストマーが第4のカーボンナノファイバーの相互に侵入し、かつ、エラストマーの特定の部分が化学的相互作用によって第4のカーボンナノファイバーの活性の高い部分と結合する。第4のカーボンナノファイバーの表面が例えば酸化処理によって適度に活性が高いと、特にエラストマー分子と結合し易くなることができる。次に、エラストマーに強い剪断力が作用すると、エラストマー分子の移動に伴って第4のカーボンナノファイバーも移動し、さらに剪断後の弾性によるエラストマーの復元力によって、凝集していた第4のカーボンナノファイバーが分離されて、エラストマー中に分散されることになる。本実施の形態によれば、炭素繊維複合材料が狭いロール間から押し出された際に、エラストマーの弾性による復元力で炭素繊維複合材料はロール間隔より厚く変形する。その変形は、強い剪断力の作用した炭素繊維複合材料をさらに複雑に流動させ、第4のカーボンナノファイバーをエラストマー中に分散させると推測できる。そして、一旦分散した第4のカーボンナノファイバーは、エラストマーとの化学的相互作用によって再凝集することが防止され、良好な分散安定性を有することができる。
エラストマーに第4のカーボンナノファイバーを剪断力によって分散させる工程(d)は、前記オープンロール法に限定されず、密閉式混練法あるいは多軸押出し混練法を用いることもできる。要するに、この工程では、凝集した第4のカーボンナノファイバーを分離できる剪断力をエラストマーに与えることができればよい。特に、オープンロール法は、ロール温度の管理だけでなく、混合物の実際の温度を測定し管理することができる。
工程(d)は、薄通し後の分出しされた炭素繊維複合材料に架橋剤を混合し、架橋して架橋体の炭素繊維複合材料としてもよい。また、炭素繊維複合材料は、架橋させずに成形してもよい。炭素繊維複合材料は、オープンロール法によって得られたシート状のままでもよいし、工程(d)で得られた炭素繊維複合材料を一般に採用されるゴムの成形加工例えば、射出成形法、トランスファー成形法、プレス成形法、押出成形法、カレンダー加工法などによって所望の形状例えばシート状に成形してもよい。
本実施の形態にかかる工程(d)において、通常、エラストマーの加工で用いられる配合剤を加えることができる。配合剤としては公知のものを用いることができる。配合剤としては、例えば、架橋剤、加硫剤、加硫促進剤、加硫遅延剤、軟化剤、可塑剤、硬化剤、補強剤、充填剤、老化防止剤、着色剤などを挙げることができる。これらの配合剤は、例えばオープンロールにおける第4のカーボンナノファイバーの投入前にエラストマーに投入することができる。
More specifically, when the elastomer and the fourth carbon nanofiber are mixed with an open roll, the viscous elastomer penetrates into the fourth carbon nanofiber, and a specific portion of the elastomer is chemically interlinked. By action, it binds to the highly active part of the fourth carbon nanofiber. When the surface of the fourth carbon nanofiber is moderately high by, for example, oxidation treatment, it can be easily bonded to an elastomer molecule. Next, when a strong shearing force acts on the elastomer, the fourth carbon nanofibers move with the movement of the elastomer molecules, and further, the aggregated fourth carbon nanofibers are recovered by the restoring force of the elastomer due to elasticity after shearing. The fibers will be separated and dispersed in the elastomer. According to the present embodiment, when the carbon fiber composite material is extruded from between narrow rolls, the carbon fiber composite material is deformed thicker than the roll interval due to the restoring force due to the elasticity of the elastomer. The deformation can be presumed to cause the carbon fiber composite material with a strong shear force to flow more complicatedly and disperse the fourth carbon nanofibers in the elastomer. The fourth carbon nanofibers once dispersed are prevented from reaggregating due to chemical interaction with the elastomer, and can have good dispersion stability.
The step (d) of dispersing the fourth carbon nanofibers in the elastomer by a shearing force is not limited to the open roll method, and a closed kneading method or a multiaxial extrusion kneading method can also be used. In short, in this step, it is sufficient that a shearing force capable of separating the aggregated fourth carbon nanofibers can be given to the elastomer. In particular, the open roll method can measure and manage the actual temperature of the mixture as well as the roll temperature.
In the step (d), a cross-linking carbon fiber composite material mixed with a cross-linking agent may be mixed and cross-linked to obtain a cross-linked carbon fiber composite material. Further, the carbon fiber composite material may be molded without being crosslinked. The carbon fiber composite material may remain in the form of a sheet obtained by the open roll method, or a rubber molding process generally employed by the carbon fiber composite material obtained in the step (d), for example, injection molding method, transfer molding. A desired shape such as a sheet may be formed by a method, a press molding method, an extrusion molding method, a calendering method, or the like.
In the step (d) according to the present embodiment, a compounding agent usually used for processing an elastomer can be added. A well-known thing can be used as a compounding agent. Examples of the compounding agent include a crosslinking agent, a vulcanizing agent, a vulcanization accelerator, a vulcanization retarder, a softening agent, a plasticizer, a curing agent, a reinforcing agent, a filler, an antiaging agent, and a coloring agent. it can. These compounding agents can be added to the elastomer before the fourth carbon nanofibers in the open roll, for example.

 なお、本実施の形態にかかる炭素繊維複合材料の製造方法においては、ゴム弾性を有した状態のエラストマーに第4のカーボンナノファイバーを直接混合したが、これに限らず、以下の方法を採用することもできる。まず、第4のカーボンナノファイバーを混合する前に、エラストマーを素練りしてエラストマーの分子量を低下させる。エラストマーは、素練りによって分子量が低下すると、粘度が低下するため、凝集した第4のカーボンナノファイバーの空隙に浸透しやすくなる。原料となるエラストマーは、パルス法NMRを用いてハーンエコー法によって30℃、観測核がHで測定した、未架橋体における、ネットワーク成分の第1のスピン−スピン緩和時間(T2n)が100~3000μ秒のゴム状弾性体である。この原料のエラストマーを素練りしてエラストマーの分子量を低下させ、第1のスピン−スピン緩和時間(T2n)が3000μ秒を越える液体状のエラストマーを得る。なお、素練り後の液体状のエラストマーの第1のスピン−スピン緩和時間(T2n)は、素練りする前の原料のエラストマーの第1のスピン−スピン緩和時間(T2n)の5~30倍であることができる。この素練りは、エラストマーが固体状態のままで行なう一般的な素練りとは異なり、強剪断力を例えばオープンロール法で与えることによってエラストマーの分子を切断し分子量を著しく低下させ、混練に適さない程の流動を示すまで、例えば液体状態になるまで行なわれる。この素練りは、例えばオープンロール法を用いた場合、ロール温度20℃(素練り時間最短60分)~150℃(素練り時間最短10分)で行なわれロール間隔dは例えば0.5mm~1.0mmで、素練りして液体状態のエラストマーに第4のカーボンナノファイバーを投入する。しかしながら、エラストマーは液体状で弾性が著しく低下しているため、エラストマーのフリーラジカルと第4のカーボンナノファイバーが結びついた状態で混練しても凝集した第4のカーボンナノファイバーはあまり分散されない。
そこで、液体状のエラストマーと第4のカーボンナノファイバーとを混合して得られた混合物中におけるエラストマーの分子量を増大させ、エラストマーの弾性を回復させてゴム状弾性体の混合物を得た後、先に説明したオープンロール法の薄通しなどを実施して第4のカーボンナノファイバーをエラストマー中に均一に分散させる。エラストマーの分子量が増大した混合物は、パルス法NMRを用いてハーンエコー法によって30℃、観測核がHで測定した、ネットワーク成分の第1のスピン−スピン緩和時間(T2n)が3000μ秒以下のゴム状弾性体である。また、エラストマーの分子量が増大したゴム状弾性体の混合物の第1のスピン−スピン緩和時間(T2n)は、素練りする前の原料エラストマーの第1のスピン−スピン緩和時間(T2n)の0.5~10倍であることができる。ゴム状弾性体の混合物の弾性は、エラストマーの分子形態(分子量で観測できる)や分子運動性(T2nで観測できる)によって表すことができる。エラストマーの分子量を増大させる工程は、混合物を加熱処理例えば40℃~100℃に設定された加熱炉内に混合物を配置し、10時間~100時間行なわれることができる。このような加熱処理によって、混合物中に存在するエラストマーのフリーラジカル同士の結合などによって分子鎖が延長され、分子量が増大する。また、エラストマーの分子量の増大を短時間で実施する場合には、架橋剤を少量、例えば架橋剤の適量の1/2以下を混合させておき、混合物を加熱処理(例えばアニーリング処理)し架橋反応によって短時間で分子量を増大させることもできる。架橋反応によってエラストマーの分子量を増大させる場合には、この後の工程で混練が困難にならない程度に架橋剤の配合量、加熱時間及び加熱温度を設定することができる。
ここで説明した工程(d)によれば、第4のカーボンナノファイバーを投入する前にエラストマーの粘性を低下させることで、エラストマー中に第4のカーボンナノファイバーをより均一に分散させることができる。より詳細には、先に説明した製造方法のように分子量が大きいエラストマーに第4のカーボンナノファイバーを混合するよりも、分子量が低下した液体状のエラストマーを用いた方が凝集した第4のカーボンナノファイバーの空隙に侵入しやすく、薄通しの工程において第4のカーボンナノファイバーをより均一に分散させることができる。また、エラストマーが分子切断されることで大量に生成されたエラストマーのフリーラジカルが第4のカーボンナノファイバーの適度に酸化された表面とより強固に結合することができるため、さらに第4のカーボンナノファイバーを均一に分散させることができる。したがって、ここで説明した工程(d)によれば、先に説明した工程(d)よりも少量の第4のカーボンナノファイバーでも同等の性能を得ることができ、高価な第4のカーボンナノファイバーを節約することで経済性も向上する。
In addition, in the manufacturing method of the carbon fiber composite material according to the present embodiment, the fourth carbon nanofiber is directly mixed with the elastomer having a rubber elasticity, but the present invention is not limited to this, and the following method is adopted. You can also First, before mixing the fourth carbon nanofiber, the elastomer is masticated to lower the molecular weight of the elastomer. Since the viscosity of the elastomer decreases when the molecular weight decreases due to mastication, the elastomer easily penetrates into the voids of the aggregated fourth carbon nanofibers. The elastomer used as a raw material has a first spin-spin relaxation time (T2n) of the network component in an uncrosslinked body measured at 30 ° C. by a Hahn-echo method using pulsed NMR with an observation nucleus of 1 H. It is a rubber-like elastic body of 3000 μsec. The raw material elastomer is masticated to lower the molecular weight of the elastomer, and a liquid elastomer having a first spin-spin relaxation time (T2n) exceeding 3000 μsec is obtained. The first spin-spin relaxation time (T2n) of the liquid elastomer after mastication is 5 to 30 times the first spin-spin relaxation time (T2n) of the raw material elastomer before mastication. Can be. This mastication is not suitable for kneading, unlike the general mastication performed while the elastomer remains in a solid state, by applying a strong shearing force by, for example, the open roll method to cut the molecular weight of the elastomer and significantly reduce the molecular weight. The process is performed until the fluid reaches a certain level, for example, until it reaches a liquid state. For example, when the open roll method is used, this mastication is performed at a roll temperature of 20 ° C. (minimum mastication time 60 minutes) to 150 ° C. (minimum mastication time 10 minutes), and the roll interval d is 0.5 mm to 1 for example. The fourth carbon nanofibers are put into a liquid elastomer that is masticated at 0.0 mm. However, since the elastomer is in a liquid state and its elasticity is remarkably reduced, the aggregated fourth carbon nanofibers are not dispersed so much even when kneaded in a state where the elastomer free radicals and the fourth carbon nanofibers are combined.
Therefore, after increasing the molecular weight of the elastomer in the mixture obtained by mixing the liquid elastomer and the fourth carbon nanofibers, restoring the elasticity of the elastomer to obtain a rubber-like elastic mixture, The fourth carbon nanofibers are uniformly dispersed in the elastomer by performing the thinning of the open roll method described in the above. The mixture having an increased molecular weight of the elastomer has a first spin-spin relaxation time (T2n) of 3000 μsec or less as measured by a Hahn-echo method using pulsed NMR at 30 ° C. and an observation nucleus of 1 H. It is a rubber-like elastic body. The first spin-spin relaxation time (T2n) of the rubber-like elastic mixture having an increased molecular weight of the elastomer is 0. It can be 5 to 10 times. The elasticity of the rubber-like elastic mixture can be represented by the molecular form of the elastomer (observable by molecular weight) and molecular mobility (observable by T2n). The step of increasing the molecular weight of the elastomer can be performed for 10 hours to 100 hours by placing the mixture in a heating furnace set to a heat treatment, for example, 40 ° C. to 100 ° C. By such a heat treatment, the molecular chain is extended by the bond between the free radicals of the elastomer present in the mixture, and the molecular weight is increased. When the molecular weight of the elastomer is increased in a short time, a small amount of a cross-linking agent, for example, ½ or less of an appropriate amount of the cross-linking agent is mixed, and the mixture is subjected to a heat treatment (for example, an annealing treatment) to perform a cross-linking reaction. The molecular weight can be increased in a short time. When the molecular weight of the elastomer is increased by a crosslinking reaction, the amount of crosslinking agent, the heating time, and the heating temperature can be set to such an extent that kneading is not difficult in the subsequent steps.
According to the step (d) described here, the fourth carbon nanofibers can be more uniformly dispersed in the elastomer by reducing the viscosity of the elastomer before introducing the fourth carbon nanofibers. . More specifically, the fourth carbon is agglomerated by using a liquid elastomer having a reduced molecular weight, rather than mixing the fourth carbon nanofiber with an elastomer having a large molecular weight as in the production method described above. The fourth carbon nanofibers can be dispersed more uniformly in the thinning process because it easily penetrates into the voids of the nanofibers. In addition, since the elastomer free radicals produced in large quantities by molecular cleavage of the elastomer can bind more firmly to the moderately oxidized surface of the fourth carbon nanofibers, the fourth carbon nanofibers are further bonded. The fiber can be uniformly dispersed. Therefore, according to the step (d) described here, the same performance can be obtained with a small amount of the fourth carbon nanofiber than in the step (d) described above, and the expensive fourth carbon nanofiber is obtained. Saving money will also improve economic efficiency.

 (IV)炭素繊維複合材料
次に、工程(d)によって得られた炭素繊維複合材料について説明する。
炭素繊維複合材料は、エラストマー100質量部に対して、機械的作用により分岐部を減らしかつ酸化したカーボンナノファイバーを20質量部~100質量部含み、200℃、10Hzにおける動的弾性率(E’)が10MPa~1000MPaであって、体積固有抵抗値が10Ω・cm~1018Ω・cmである。炭素繊維複合材料は、エラストマーと、該エラストマー中に均一に分散した第4のカーボンナノファイバーと、を含むことができる。
一般に、エラストマーやプラスチックなどは、室温での体積固有抵抗値が1012(Ω・cm)を超えるものが多く、絶縁性の高いもので体積固有抵抗値が1018(Ω・cm)程度の電気絶縁性を有している。しかしながら、一般に市販されているカーボンナノファイバー、例えば気相成長炭素繊維などをエラストマーに均一に分散させて配合した場合、気相成長炭素繊維が比較的少量であっても10(Ω・cm)程度の体積固有抵抗値を示すことがわかっている。つまり、カーボンナノファイバーによってエラストマーを補強しようとすると、エラストマーの絶縁性を維持することができなくなり、補強と絶縁性とを同時に得ることが難しいということが従来の技術常識であった。なお、本実施形態において体積固有抵抗値といえば、室温におけるJIS−7194に準拠して四探針法により測定された値をいうものとする。
本実施の形態における炭素繊維複合材料は、比較的大量に第4のカーボンナノファイバーを配合しかつ均一に分散させて所望の強度を得ても、電気伝導し難く、体積固有抵抗値が高いものであることができる。炭素繊維複合材料は、カーボンナノファイバーの補強により高い強度や耐熱性を有することができ、しかも、ゴム材料としての電気絶縁性を要求される用途にも採用することが可能になる。必要とされる電気絶縁性は、ゴム材料の用途にもよるが、例えば体積固有抵抗値が10(Ω・cm)以上を要求される場合があり、特に体積固有抵抗値が10(Ω・cm)以上を要求されることが多く、これらの用途にも適用可能である。
油田用途の絶縁性物品は、炭素繊維複合材料を含むことができる。電子部品は、前記絶縁性物品を含むことができる。検層装置は、筐体と、該筐体内に配置された前記電子部品と、を備えることができる。
体積固有抵抗値が10(Ω・cm)以上を要求される用途としては、例えば油田に用いられる検層装置におけるアナログ信号を用いた通信において有効であり、体積固有抵抗値が10(Ω・cm)以上を要求される用途としては、例えば検層装置におけるデジタル信号を用いた通信において有効であり、通信速度を上げるためにはさらに体積固有抵抗値が10(Ω・cm)以上を要求されることがあり、特に、体積固有抵抗値が10(Ω・cm)以上を要求されることがある。炭素繊維複合材料は、体積固有抵抗値が10Ω・cm~1018Ω・cmであり、10Ω・cm~1018Ω・cmであることができ、さらには10Ω・cm~1018Ω・cmであることができ、特に10Ω・cm~1018Ω・cmであることができる。例えば、工程(b)で圧縮処理を採用した第4のカーボンナノファイバーと、エラストマーに含フッ素エラストマーと、を用いた炭素繊維複合材料は、200℃における動的弾性率(E’)が15MPa~300MPaであって、体積固有抵抗値が1011Ω・cm~1018Ω・cmであることができる。例えば、工程(b)で圧縮処理を採用した第4のカーボンナノファイバーと、エラストマーにエチレン−プロピレンゴムと、を用いた炭素繊維複合材料は、200℃における動的弾性率(E’)が10MPa~200MPaであって、体積固有抵抗値が10Ω・cm~1018Ω・cmであることができる。例えば、工程(b)で粉砕処理を採用した第4のカーボンナノファイバーと、エラストマーにエチレン−プロピレンゴムと、を用いた炭素繊維複合材料は、200℃における動的弾性率(E’)が10MPa~200Mpaであって、体積固有抵抗値が10Ω・cm~1018Ω・cmであることができる。なお、本実施の形態において動的弾性率(E’)は、JIS K6394に基づいて動的粘弾性試験を行って測定されるものとする。
(IV) Carbon fiber composite material Next, the carbon fiber composite material obtained by the step (d) will be described.
The carbon fiber composite material contains 20 to 100 parts by mass of carbon nanofibers that are reduced by mechanical action and oxidized to 100 parts by mass of the elastomer, and has a dynamic elastic modulus (E ′ at 200 ° C. and 10 Hz). ) Is 10 MPa to 1000 MPa, and the volume resistivity is 10 6 Ω · cm to 10 18 Ω · cm. The carbon fiber composite material can include an elastomer and fourth carbon nanofibers uniformly dispersed in the elastomer.
In general, many elastomers and plastics have a volume resistivity exceeding 10 12 (Ω · cm) at room temperature, and are highly insulating and have a volume resistivity of about 10 18 (Ω · cm). Insulation. However, when carbon nanofibers that are commercially available, such as vapor-grown carbon fibers, are uniformly dispersed in the elastomer and blended, even if the vapor-grown carbon fibers are relatively small, 10 1 (Ω · cm) It has been found that it exhibits a volume resistivity value of some degree. In other words, it has been a conventional technical common sense that when an attempt is made to reinforce an elastomer with carbon nanofibers, the insulation of the elastomer cannot be maintained, and it is difficult to obtain reinforcement and insulation at the same time. In this embodiment, the volume resistivity value is a value measured by the four-probe method in accordance with JIS-7194 at room temperature.
The carbon fiber composite material in the present embodiment has a high volume resistivity value, even if a relatively large amount of the fourth carbon nanofiber is blended and evenly dispersed to obtain a desired strength, making it difficult to conduct electricity. Can be. The carbon fiber composite material can have high strength and heat resistance due to the reinforcement of the carbon nanofibers, and can also be used for applications that require electrical insulation as a rubber material. The required electrical insulation depends on the use of the rubber material, but for example, a volume resistivity value of 10 6 (Ω · cm) or more may be required, and in particular, a volume resistivity value of 10 7 (Ω · Cm) or more is often required, and can be applied to these applications.
Insulating articles for oil field applications can include carbon fiber composite materials. The electronic component can include the insulating article. The well logging apparatus can include a housing and the electronic component disposed in the housing.
The application requiring a volume resistivity of 10 6 (Ω · cm) or more is effective, for example, in communication using an analog signal in a logging apparatus used in an oil field, and the volume resistivity is 10 7 (Ω As an application requiring cm) or more, for example, it is effective in communication using a digital signal in a logging device, and in order to increase the communication speed, the volume specific resistance value should be 10 8 (Ω · cm) or more. In particular, the volume resistivity value may be required to be 10 9 (Ω · cm) or more. The carbon fiber composite material has a volume resistivity value of 10 6 Ω · cm to 10 18 Ω · cm, and can be 10 7 Ω · cm to 10 18 Ω · cm, and more preferably 10 8 Ω · cm It can be 10 18 Ω · cm, in particular 10 9 Ω · cm to 10 18 Ω · cm. For example, a carbon fiber composite material using the fourth carbon nanofiber that has been subjected to compression treatment in the step (b) and a fluorine-containing elastomer as an elastomer has a dynamic elastic modulus (E ′) at 200 ° C. of 15 MPa ~ It can be 300 MPa, and the volume resistivity value can be 10 11 Ω · cm to 10 18 Ω · cm. For example, the carbon fiber composite material using the fourth carbon nanofiber that has been subjected to compression treatment in the step (b) and the ethylene-propylene rubber as the elastomer has a dynamic elastic modulus (E ′) at 200 ° C. of 10 MPa. The volume resistivity value may be 10 7 Ω · cm to 10 18 Ω · cm. For example, the carbon fiber composite material using the fourth carbon nanofibers that have been pulverized in the step (b) and the ethylene-propylene rubber as the elastomer has a dynamic elastic modulus (E ′) at 200 ° C. of 10 MPa. The volume resistivity value may be 10 8 Ω · cm to 10 18 Ω · cm. In this embodiment, the dynamic elastic modulus (E ′) is measured by performing a dynamic viscoelasticity test based on JIS K6394.

 炭素繊維複合材料は、パルス法NMRを用いてハーンエコー法によって150℃、観測核がHで測定した、無架橋体における、第1のスピン−スピン緩和時間(T2n)は100~3000μ秒であり、第2のスピン−スピン緩和時間を有する成分の成分分率(fnn)は0~0.2であることができる。炭素繊維複合材料の150℃で測定したT2n及びfnnは、マトリックスであるエラストマーに第4のカーボンナノファイバーが均一に分散されていることを表すことができる。つまり、エラストマーに第4のカーボンナノファイバーが均一に分散されているということは、エラストマーが第4のカーボンナノファイバーによって拘束されている状態であるともいえる。この状態では、第4のカーボンナノファイバーによって拘束を受けたエラストマー分子の運動性は、第4のカーボンナノファイバーの拘束を受けない場合に比べて小さくなる。そのため、炭素繊維複合材料の第1のスピン−スピン緩和時間(T2n)、第2のスピン−スピン緩和時間(T2nn)及びスピン−格子緩和時間(T1)は、第4のカーボンナノファイバーを含まないエラストマー単体の場合より短くなり、特に第4のカーボンナノファイバーが均一に分散することでより短くなる。
また、エラストマー分子が第4のカーボンナノファイバーによって拘束された状態では、以下の理由によって、非ネットワーク成分(非網目鎖成分)は減少すると考えられる。すなわち、第4のカーボンナノファイバーによってエラストマーの分子運動性が全体的に低下すると、非ネットワーク成分は容易に運動できなくなる部分が増えて、ネットワーク成分と同等の挙動をしやすくなること、また、非ネットワーク成分(末端鎖)は動きやすいため、第4のカーボンナノファイバーの活性点に吸着されやすくなること、などの理由によって、非ネットワーク成分は減少すると考えられる。そのため、第2のスピン−スピン緩和時間(T2nn)を有する成分の成分分率(fnn)は、fn+fnn=1であるので、第4のカーボンナノファイバーを含まないエラストマー単体の場合より小さくなる。したがって、炭素繊維複合材料は、パルス法NMRを用いてハーンエコー法によって得られる測定値が上記の範囲にあることによって第4のカーボンナノファイバーが均一に分散されていることがわかる。
また、第4のカーボンナノファイバーの周囲には、エラストマーの一部が混練中に分子鎖切断され、それによって生成されたフリーラジカルが第4のカーボンナノファイバーの表面をアタックして吸着したエラストマー分子の凝集体と考えられる界面相が形成される。界面相は、例えばエラストマーとカーボンブラックとを混練した際にカーボンブラックの周囲に形成されるバウンドラバーに類似するものと考えられる。このような界面相は、第4のカーボンナノファイバーを被覆して保護し、また、カーボンナノファイバーを所定量以上配合することで界面相同士が連鎖した界面相に囲まれてナノメートルサイズに分割されたエラストマーの小さなセルを形成すると推定される。このような小さなセルが炭素繊維複合材料の全体にほぼ均質に形成されることで、単に2つの材料を複合したことによる効果を超えた効果を期待することができる。
The carbon fiber composite material has a first spin-spin relaxation time (T2n) of 100 to 3000 μsec in a non-crosslinked body, measured at 150 ° C. by the Hahn echo method using pulsed NMR, and the observation nucleus is 1 H. And the component fraction (fnn) of the component having the second spin-spin relaxation time can be 0 to 0.2. T2n and fnn measured at 150 ° C. of the carbon fiber composite material can represent that the fourth carbon nanofibers are uniformly dispersed in the matrix elastomer. That is, the fact that the fourth carbon nanofibers are uniformly dispersed in the elastomer can be said to be a state where the elastomer is constrained by the fourth carbon nanofibers. In this state, the mobility of the elastomer molecules constrained by the fourth carbon nanofibers is smaller than that when not constrained by the fourth carbon nanofibers. Therefore, the first spin-spin relaxation time (T2n), the second spin-spin relaxation time (T2nn), and the spin-lattice relaxation time (T1) of the carbon fiber composite material do not include the fourth carbon nanofiber. It becomes shorter than the case of the elastomer alone, and particularly becomes shorter when the fourth carbon nanofibers are uniformly dispersed.
In addition, in the state where the elastomer molecules are constrained by the fourth carbon nanofibers, it is considered that the non-network component (non-network chain component) decreases for the following reason. That is, when the molecular mobility of the elastomer is lowered overall by the fourth carbon nanofibers, the non-network component cannot easily move, and the behavior becomes the same as that of the network component. Since the network component (terminal chain) is easy to move, the non-network component is considered to decrease due to the fact that it is easily adsorbed to the active point of the fourth carbon nanofiber. Therefore, since the component fraction (fnn) of the component having the second spin-spin relaxation time (T2nn) is fn + fnn = 1, it is smaller than the case of the elastomer alone not including the fourth carbon nanofiber. Therefore, it can be seen that in the carbon fiber composite material, the fourth carbon nanofibers are uniformly dispersed when the measurement value obtained by the Hahn echo method using the pulse method NMR is in the above range.
In addition, around the fourth carbon nanofiber, an elastomer molecule in which a part of the elastomer is subjected to molecular chain cleavage during kneading, and free radicals generated thereby attack and adsorb the surface of the fourth carbon nanofiber. An interfacial phase that is considered to be an aggregate is formed. The interfacial phase is considered to be similar to bound rubber formed around carbon black when, for example, an elastomer and carbon black are kneaded. Such an interfacial phase is coated and protected by covering the fourth carbon nanofibers, and by blending more than a predetermined amount of carbon nanofibers, the interfacial phases are surrounded by an interfacial phase and divided into nanometer sizes. It is presumed to form small cells of the resulting elastomer. By forming such small cells almost uniformly throughout the carbon fiber composite material, it is possible to expect an effect that exceeds the effect of simply combining the two materials.

 (V)検層装置
図7は、本発明の一実施形態にかかる海底用途の検層装置を模式的に示す断面図である。図8は、本発明の一実施形態にかかる図7における検層装置の筐体を模式的に示す断面図である。図9は、本発明の一実施形態にかかる地下用途の検層装置を模式的に示す断面図である。
検層装置(logging tool)は、例えば掘削された坑井(borehole)内及び坑井周辺の地層、油層などの物理的特性や坑井あるいはケーシングの幾何学的特性(孔径、方位、傾斜等)、油層の流れの挙動などを深度毎に記録するための装置であって、例えば油田(oilfield)において用いることができる。油田用途の検層装置としては、例えば、図7,8に示す海底(subsea)用途と、図9に示す地下(underground)用途と、が挙げることができる。検層装置には、ワイヤーライン検層(Wireline log/logging)や泥水検層(Mud logging)などがあり、測定機器が掘削アッセンブリーに装備されている掘削中検層(LWD:Logging While Drilling)や掘削中測定(MWD:Measurement While Drilling)などがあるが、ここではワイヤーライン検層に用いる検層装置について説明する。
図7に示すように、海洋でのワイヤーライン検層を用いた地下資源の探査は、例えば海152に浮くプラットホーム150から海底154に設けられた縦穴や横穴などで構成される坑井156内に検層装置として例えばダウンホール装置(Downhole Apparatus)160を進入させ、地中の地質構造などを探査し、目標物質である例えば石油の有無を探査する。ダウンホール装置160は、例えばプラットホームから延びる長いケーブルもしくはコミュニケーション・リンクの先端に固定され、図8に示すような複数の圧力容器などの筐体161を内部に有する。筐体161の内部には、例えば電気検層(SP検層、ノルマル検層、インダクション検層、ラテロ検層、マイクロ比抵抗検層など)、放射能検層(ガンマ線検層、中性子検層、密度検層、核磁気共鳴検層など)、音波検層(音波(音響)検層、アレー・音波検層、セメント・ボンド検層など)、地質情報検層(ディップメーター、FMIなど)、震探検層(チェックショット速度検層、VSPなど)、サンプリング検層(サイドウォール・コアリング検層、RFT,MDTなど)、補助検層(キャリパー(坑径)測定、坑井幾何学特性検層、温度検層など)、特別検層(過酷条件下での検層(Logs in hostile environment)、掘削管経由検層(measurement through drill pipe)など)などの探査用電子機器が探査の目的に合わせて選択して封入されて配置され、地中の地質構造などを探査することが可能であるが、地下深く掘削された坑井156内部では高温にさらされるとともに、坑井156へ進入する際の振動や衝撃を受けるため、筐体161内の電子機器にも高い耐熱性と高い強度が要求される。
筐体161の内部には、電気コネクタ162が例えば複数配置され、あるいは、複数の筐体161がその端部内に形成された電気コネクタ162によって互いに連結されている。電気コネクタ162は、互いに離間配置された複数のピン162aと、複数のピン162aを固定する支持部162bと、を含み、支持部162bは、炭素繊維複合材料によって形成することができ、例えば図8の筐体161の両端部に配置された電気コネクタ162のように炭素繊維複合材料で形成した支持部162bによって複数のピン162a間の絶縁性を維持したまま固定することができる。電気コネクタ162のピン162aは、ダウンホール装置160振動や衝撃を受け、あるいは電線163に接続される場合にはその電線163が振動で振れるため、ピン162aを確実に固定する強度が要求されるが、炭素繊維複合材料によってピン162aを固定することで坑井156内の高温の過酷な環境においても比較的長時間利用可能であり、しかもカーボンナノファイバーで補強しているにもかかわらず例えば一般にピン間に要求される体積固有抵抗値10(Ω・cm)以上の絶縁性能を有することができる。また、電気コネクタ162の支持部162bは、筐体161におけるフィードスルー(feedthrough)として機能することができる。フィードスルーは、例えば米国特許第7,226,312号に示され、参考文献としてここに援用する。
また、筐体161の内部には、複数の電線163が配置され、例えば電気コネクタ162のピン162aなどに接続されている。電線163は、例えば芯材として導電性金属の導線と、導線を被覆した被覆部と、を含み、被覆部は、炭素繊維複合材料によって形成することができる。このように炭素繊維複合材料で被覆された電線163は、ダウンホール装置160の高温の過酷な環境下における振動や衝撃に耐え、かつ、絶縁性を有することができる。電線は、例えば米国特許第6,446,723号に示され、参考文献としてここに援用する。
さらに、筐体161に接続されて該筐体161の外部に延びる、電線などの複数の芯線を束ねたケーブル164が配置されている。ケーブル164は、芯線と、該芯線を被覆した被覆部と、を含み、被覆部は、炭素繊維複合材料によって形成することができる。ケーブル164の芯線は、複数の芯線例えば電線で形成することができる。このようなケーブル164は、ワイヤーライン検層においては地下にある筐体161と地上にあるデータ取得システムとの間でのデータやコマンドの送受信や電力を筐体161内の電子機器に送る役割を有することができる。このようなケーブル164は、坑井156内に延びるロッド内面との接触による摩耗や破断に耐え、かつ、絶縁性を有することができる。ケーブルは、例えば米国特許第7,259,331号に示され、参考文献としてここに援用する。
また、筐体161の内部には、例えば複数のコイル165が配置され、これらコイル165にはマグネットワイヤが巻きつけられている。マグネットワイヤは、コイルワイヤと呼ばれることもある。このマグネットワイヤは、導線と、該導線を被覆した被覆部と、を含み、被覆部は、炭素繊維複合材料によって形成することができる。被覆部は、炭素繊維複合材料を用いることで薄い絶縁被膜として形成され、ダウンホール装置160の高温の過酷な環境下における振動や衝撃に耐え、かつ、絶縁性を有することができる。マグネットワイヤを炭素繊維複合材料によって被覆することによって、絶縁性を維持しながら、第4のカーボンナノファイバーによる伝熱効果によって効果的に放熱することができる。マグネットワイヤは、例えば米国特許第6,898,997号に示され、参考文献としてここに援用する。
さらに、筐体161の内部には、例えば複数の電子部品167を配置した電気基板166が配置されている。
また、筐体161の内部には、例えば複数の電子部品167の自己発熱による過熱を防止するため、放熱シート167aを配置することができる。放熱シート167aは、ヒートシンクとも呼ばれ、例えば電子部品167の表面に接触して、図8においては電子部品167と電気基板166との間に配置されているが、電気基板166とは反対側の電子部品167の表面に接触するように配置することもできる。放熱シート167aを炭素繊維複合材料によって形成することによって、電子部品167との絶縁性を維持しながら、第4のカーボンナノファイバーによる伝熱効果によって効果的に放熱することができる。さらに、この放熱シート167aを免振シートとして用いることもでき、電子部品167の耐衝撃性を向上させることができる。放熱シートは、例えば米国特許公開2008/0223579号に示され、参考文献としてここに援用する。免振シートは、例えば米国特許第6,280,874号、米国特許公開第2009/0183941号、及び米国特許公開第2009/0151589号に示され、参考文献としてここに援用する。
さらに、筐体161内に配置された電子部品167や筐体161の壁部161a内に埋め込まれた電子部品(センサ168)は、炭素繊維複合材料によって全体を覆うように封入することができる。このように電子部品167の全体を炭素繊維複合材料によって防水構造とすることができる。例えば、センサ168は、センサ168に接続された図示しないリード線を含む電線163とともに、筐体161の壁部161aに形成された開口168a内に配置され、その開口168aを炭素繊維複合材料168bによって封入(モールドとも呼ぶことがある)されている。また、図示していないが、電気基板166上の電子部品167の全体を覆うように電子部品167を炭素繊維複合材料内に封入してもよい。このように炭素繊維複合材料168bによって覆われたセンサ168や電子部品167は、筐体161の外部や筐体161内部の水分に対して防水構造をとるとともに、絶縁性能を有することができる。
なお、炭素繊維複合材料を用いた前記各部品における強度や絶縁性などの要求性能に応じて第4のカーボンナノファイバーの配合量やその他の配合剤例えばカーボンブラックなどを適宜配合することができる。また、図7,8を用いて説明した検層装置は、本発明の一実施形態であって、図8では筐体161、電気コネクタ162、ケーブル164、コイル165、電気基板166、放熱シート167a、及び防水構造を1つの検層装置に組み込んだ例を説明したが、これに限らず、検層用途に合わせて選択して組み込むことができる。
図9に示すように、地表153でのワイヤーライン検層を用いた地下資源の探査は、例えば検層トラック151aやウインチ151bなどで構成された地上装置151と、ウインチ151bから坑井156内に延びるワイヤーライン155の先端に固定された例えばダウンホール装置(Downhole Apparatus)160によって行うことができる。ダウンホール装置160については、前記海底用途の検層装置と基本的には同様であるので、ここでは説明を省略する。
(V) Log Logging Device FIG. 7 is a cross-sectional view schematically showing a log logging device for seabed use according to an embodiment of the present invention. FIG. 8 is a cross-sectional view schematically showing a case of the logging apparatus in FIG. 7 according to one embodiment of the present invention. FIG. 9 is a cross-sectional view schematically showing an underground logging tool according to an embodiment of the present invention.
The logging tool is a physical property of the formation, oil layer, etc. in the borehole and around the well and the geometric properties of the well or casing (bore diameter, orientation, inclination, etc.) This is a device for recording the behavior of the oil layer flow for each depth, and can be used in, for example, an oil field. Examples of the logging device for oil field use include a subsea application shown in FIGS. 7 and 8 and an underground application shown in FIG. The logging equipment includes wireline logging (muline logging) and mud logging (mud logging), etc., and logging logging (LWD) with measuring equipment installed in the drilling assembly, While there is a measurement during excavation (MWD: Measurement While Drilling), a logging system used for wireline logging will be described here.
As shown in FIG. 7, the exploration of underground resources using wireline logging in the ocean, for example, in a well 156 composed of vertical holes or horizontal holes provided in the seabed 154 from a platform 150 floating in the sea 152, for example. For example, a downhole apparatus 160 is entered as a logging apparatus, and the underground geological structure and the like are searched for, for example, the presence or absence of petroleum as a target material. The downhole device 160 is fixed to, for example, the end of a long cable or communication link extending from the platform, and has a housing 161 such as a plurality of pressure vessels as shown in FIG. Inside the casing 161, for example, electrical logging (SP logging, normal logging, induction logging, ratello logging, micro resistivity logging, etc.), radioactivity logging (gamma ray logging, neutron logging, Density logging, nuclear magnetic resonance logging, etc.), acoustic logging (acoustic (acoustic) logging, array / sonic logging, cement bond logging, etc.), geological information logging (dip meter, FMI, etc.), earthquake Exploration logging (check shot velocity logging, VSP, etc.), sampling logging (sidewall / coring logging, RFT, MDT, etc.), auxiliary logging (caliper measurement, well geometry logging) Temperature logging, etc.), Special logging (Logs in host environment, logging through drilling pipe, etc.) Which exploration electronics can be selected and enclosed according to the purpose of exploration and can be used for exploring underground geological structures, etc., but they are exposed to high temperatures inside the well 156 deeply drilled deep underground. In addition, since it receives vibration and impact when entering the well 156, the electronic equipment in the housing 161 is also required to have high heat resistance and high strength.
For example, a plurality of electrical connectors 162 are arranged inside the housing 161, or the plurality of housings 161 are connected to each other by electrical connectors 162 formed in the end portions thereof. The electrical connector 162 includes a plurality of pins 162a spaced apart from each other and a support portion 162b that fixes the plurality of pins 162a. The support portion 162b can be formed of a carbon fiber composite material, for example, FIG. It can be fixed while maintaining the insulation between the plurality of pins 162a by the support portion 162b formed of a carbon fiber composite material like the electrical connectors 162 arranged at both ends of the casing 161. The pin 162a of the electrical connector 162 is subjected to the vibration and impact of the downhole device 160, or when connected to the electric wire 163, the electric wire 163 vibrates due to the vibration, and thus the strength for securely fixing the pin 162a is required. By fixing the pin 162a with a carbon fiber composite material, the pin 162a can be used for a relatively long time even in a severe environment at a high temperature in the well 156. It can have an insulation performance of 10 6 (Ω · cm) or more, which is required between them. Further, the support portion 162 b of the electrical connector 162 can function as a feedthrough in the housing 161. Feedthroughs are shown, for example, in US Pat. No. 7,226,312 and are hereby incorporated by reference.
In addition, a plurality of electric wires 163 are arranged inside the housing 161 and connected to, for example, the pins 162 a of the electrical connector 162. The electric wire 163 includes, for example, a conductive metal conductive wire as a core material and a covering portion covering the conductive wire, and the covering portion can be formed of a carbon fiber composite material. Thus, the electric wire 163 covered with the carbon fiber composite material can withstand vibration and impact of the downhole device 160 under a severe environment at high temperature and can have insulation properties. Electrical wires are shown, for example, in US Pat. No. 6,446,723, incorporated herein by reference.
Further, a cable 164 that is connected to the casing 161 and extends to the outside of the casing 161 and in which a plurality of core wires such as electric wires are bundled is disposed. The cable 164 includes a core wire and a covering portion that covers the core wire, and the covering portion can be formed of a carbon fiber composite material. The core wire of the cable 164 can be formed of a plurality of core wires, for example, electric wires. Such a cable 164 has the role of transmitting and receiving data and commands between the case 161 in the underground and the data acquisition system on the ground and sending power to the electronic devices in the case 161 in the wireline logging. Can have. Such a cable 164 can withstand abrasion and breakage due to contact with the inner surface of the rod extending into the well 156, and can have insulating properties. Cables are shown, for example, in US Pat. No. 7,259,331, which is hereby incorporated by reference.
Further, for example, a plurality of coils 165 are arranged inside the housing 161, and a magnet wire is wound around these coils 165. The magnet wire is sometimes called a coil wire. The magnet wire includes a conductive wire and a covering portion that covers the conductive wire, and the covering portion can be formed of a carbon fiber composite material. The covering portion is formed as a thin insulating film by using a carbon fiber composite material, can withstand vibrations and impacts in a severe environment of high temperature of the downhole device 160, and can have insulating properties. By covering the magnet wire with the carbon fiber composite material, it is possible to effectively dissipate heat by the heat transfer effect of the fourth carbon nanofiber while maintaining the insulation. Magnet wires are shown, for example, in US Pat. No. 6,898,997, incorporated herein by reference.
Further, an electric board 166 on which a plurality of electronic components 167 are arranged, for example, is arranged inside the casing 161.
In addition, in the housing 161, for example, a heat dissipation sheet 167a can be disposed in order to prevent overheating due to self-heating of the plurality of electronic components 167, for example. The heat dissipating sheet 167a is also called a heat sink, and is in contact with the surface of the electronic component 167, for example, and is disposed between the electronic component 167 and the electric board 166 in FIG. It can also be arranged so as to contact the surface of the electronic component 167. By forming the heat dissipating sheet 167a from a carbon fiber composite material, it is possible to effectively dissipate heat by the heat transfer effect of the fourth carbon nanofibers while maintaining insulation from the electronic component 167. Further, the heat dissipation sheet 167a can be used as a vibration isolation sheet, and the impact resistance of the electronic component 167 can be improved. The heat dissipation sheet is shown, for example, in US Patent Publication No. 2008/0223579, which is incorporated herein by reference. Isolation sheets are shown, for example, in U.S. Patent No. 6,280,874, U.S. Patent Publication No. 2009/0183941, and U.S. Patent Publication No. 2009/0151589, which are incorporated herein by reference.
Further, the electronic component 167 arranged in the housing 161 and the electronic component (sensor 168) embedded in the wall portion 161a of the housing 161 can be encapsulated so as to cover the whole with a carbon fiber composite material. In this way, the entire electronic component 167 can be waterproofed with the carbon fiber composite material. For example, the sensor 168 is disposed in the opening 168a formed in the wall portion 161a of the housing 161 together with the electric wire 163 including a lead wire (not shown) connected to the sensor 168, and the opening 168a is formed by the carbon fiber composite material 168b. Encapsulated (sometimes called mold). Although not shown, the electronic component 167 may be enclosed in the carbon fiber composite material so as to cover the entire electronic component 167 on the electric substrate 166. As described above, the sensor 168 and the electronic component 167 covered with the carbon fiber composite material 168b can have a waterproof structure against moisture inside the housing 161 and inside the housing 161, and can have insulating performance.
In addition, the blending amount of the fourth carbon nanofibers and other compounding agents such as carbon black can be appropriately blended according to the required performance such as strength and insulation in each component using the carbon fiber composite material. 7 and 8 is an embodiment of the present invention, and in FIG. 8, a casing 161, an electrical connector 162, a cable 164, a coil 165, an electrical board 166, and a heat dissipation sheet 167a. Although the example in which the waterproof structure is incorporated in one logging device has been described, the present invention is not limited to this, and the waterproof structure can be selected and incorporated according to the logging application.
As shown in FIG. 9, the exploration of underground resources using wireline logging on the ground surface 153 is performed, for example, on the ground device 151 composed of a logging track 151a, a winch 151b, and the like, and from the winch 151b to the well 156. For example, it can be performed by a downhole apparatus 160 fixed to the tip of the extending wire line 155. The downhole device 160 is basically the same as the logging device for the seabed application, and the description thereof is omitted here.

 上記のように、本発明の実施形態について詳細に説明したが、本発明の新規事項及び効果から実体的に逸脱しない多くの変形が可能であることは当業者には容易に理解できよう。したがって、このような変形例はすべて、本発明の範囲に含まれるものとする。 As described above, the embodiments of the present invention have been described in detail. However, those skilled in the art can easily understand that many modifications can be made without departing from the novel matters and effects of the present invention. Accordingly, all such modifications are intended to be included in the scope of the present invention.

 以下、本発明の実施例について述べるが、本発明はこれらに限定されるものではない。
(1)カーボンナノファイバーの作成
(1−1)縦型加熱炉(内径17.0cm、長さ150cm)の頂部に、スプレーノズルを取り付ける。加熱炉の炉内壁温度(反応温度)を1000℃に昇温・維持し、スプレーノズルから4重量%のフェロセンを含有するベンゼンの液体原料20g/分を100L/分の水素ガスの流量で炉壁に直接噴霧(スプレー)散布するように供給する。この時のスプレーの形状は円錐側面状(ラッパ状ないし傘状)であり、ノズルの頂角が60°である。このような条件の下で、フェロセンは熱分解して鉄微粒子を作り、これがシード(種)となってベンゼンの熱分解による炭素から、第1のカーボンナノファイバーを生成成長させた。本方法で成長した第1のカーボンナノファイバーを5分間隔で掻き落としながら1時間にわたって連続的に製造した。
Examples of the present invention will be described below, but the present invention is not limited thereto.
(1) Production of carbon nanofiber (1-1) A spray nozzle is attached to the top of a vertical heating furnace (inner diameter 17.0 cm, length 150 cm). The furnace wall temperature (reaction temperature) is raised to and maintained at 1000 ° C., and 20 g / min of a benzene liquid raw material containing 4% by weight of ferrocene is supplied from the spray nozzle at a flow rate of hydrogen gas of 100 L / min. To be sprayed directly. The shape of the spray at this time is a conical side surface (trumpet shape or umbrella shape), and the apex angle of the nozzle is 60 °. Under such conditions, ferrocene was pyrolyzed to produce iron fine particles, which became seeds, and the first carbon nanofibers were produced and grown from carbon obtained by pyrolysis of benzene. The first carbon nanofibers grown by this method were continuously produced for 1 hour while scraping off at intervals of 5 minutes.

(1−2)比較例サンプルを製造するためのカーボンナノファイバーとして、黒鉛化カーボンナノファイバー(表では「S」と示す)と、粉砕処理カーボンナノファイバー(表では「SH」と示す)と、酸化処理カーボンナノファイバー(表では「SO」と示す)と、を得た。
黒鉛化カーボンナノファイバー(S)は、前記(1−1)で得られた第1のカーボンナノファイバーを、さらに不活性ガス雰囲気中において2800℃で熱処理して黒鉛化した。黒鉛化カーボンナノファイバー(S)は、平均直径87nm、平均長さ9.1μm、表面の酸素濃度2.1atm%であった。黒鉛化カーボンナノファイバー(S)は、市販されているカーボンナノファイバーであって、昭和電工社製の商品名VGCF−Sである。
粉砕処理カーボンナノファイバー(SH)は、前記黒鉛化カーボンナノファイバー(S)を、大阪ケミカル社製回転式粉砕機ワンダーブレンダーWB−1(ステンレス粉砕刃、周速度180m/s)に入れ、0.5分間粉砕処理を行って得た。
酸化処理カーボンナノファイバー(SO)は、前記黒鉛化カーボンナノファイバー(S)120gを容器(寸法は300mm×300mm×150mm)に入れ、50ml/minで大気雰囲気を連続流入した加熱炉(寸法は700mm×350mm×900mm)に入れ、表1に示す工程(c)の熱処理温度と熱処理時間で加熱炉内で保持して熱処理することで酸化処理を行って得た。なお、加熱炉内の実際の温度は、設定温度に対し±30℃の範囲であった。
(1-2) As carbon nanofibers for producing a comparative sample, graphitized carbon nanofibers (shown as “S” in the table), pulverized carbon nanofibers (shown as “SH” in the table), Oxidized carbon nanofibers (shown as “SO” in the table) were obtained.
The graphitized carbon nanofiber (S) was graphitized by further heat-treating the first carbon nanofiber obtained in (1-1) above at 2800 ° C. in an inert gas atmosphere. The graphitized carbon nanofiber (S) had an average diameter of 87 nm, an average length of 9.1 μm, and a surface oxygen concentration of 2.1 atm%. The graphitized carbon nanofiber (S) is a commercially available carbon nanofiber, and is a trade name VGCF-S manufactured by Showa Denko K.K.
For the pulverized carbon nanofiber (SH), the graphitized carbon nanofiber (S) was put into a rotary pulverizer Wonder Blender WB-1 (stainless steel pulverization blade, peripheral speed 180 m / s) manufactured by Osaka Chemical Co., Ltd. Obtained by grinding for 5 minutes.
Oxidation treated carbon nanofiber (SO) is a heating furnace (size is 700 mm) in which 120 g of graphitized carbon nanofiber (S) is put in a container (size is 300 mm × 300 mm × 150 mm) and air atmosphere is continuously introduced at 50 ml / min. × 350 mm × 900 mm), and obtained by performing an oxidation treatment by holding in a heating furnace at a heat treatment temperature and a heat treatment time in the step (c) shown in Table 1 and performing a heat treatment. The actual temperature in the heating furnace was in the range of ± 30 ° C. with respect to the set temperature.

(1−3)工程(b)で圧縮処理を用いた第4のカーボンナノファイバー(表では「SAPO」と示す)は、前記(1−1)で得られた第1のカーボンナノファイバーを、不活性ガス雰囲気中で前記気相成長法における反応温度より低温である表1に示す工程(a)の熱処理温度(1200℃)で熱処理して第2のカーボンナノファイバー(SA)を得て、第2のカーボンナノファイバー(SA)を2本のロールを有する乾式圧縮造粒機に投入して表1に示す工程(b)のロール処理を行って第3のカーボンナノファイバー(SAP)を得て、第3のカーボンナノファイバー(SAP)を大気雰囲気の加熱炉に入れ、表1に示す工程(c)の熱処理温度(650℃)と熱処理時間(2時間)で加熱炉内で保持して熱処理することで酸化処理を行って得た。なお、第4のカーボンナノファイバーの製造における工程(b)のロール処理は、第2のカーボンナノファイバー(SA)を、2本のロールを有する乾式圧縮造粒機に投入して得た。乾式圧縮造粒機はロールプレス機(ロール径は150mm、ロールは平滑ロール、ロール間隔は0mm、ロール間の設定圧縮力(線圧)は1960N/cm、ギア比1:1.3、ロール回転数3rpm)であった。ロール処理カーボンナノファイバーは、直径が約2~3cmの板状の塊(カーボンナノファイバー集合体)に造粒された。その造粒された板状の塊をさらに、8枚の回転刃を有する破砕造粒整粒機(回転数15rpm、スクリーン5mm)を通して破砕し、粒径を整えた。また、第4のカーボンナノファイバーの製造における工程(c)の酸化処理は、前記酸化処理カーボンナノファイバー(SO)の製造条件と同様であったのでここでの説明は省略する。
工程(b)で粉砕処理を用いた第4のカーボンナノファイバー(表では「SAHO」と示す)は、前記(1−1)で得られた第1のカーボンナノファイバーを、不活性ガス雰囲気中で前記気相成長法における反応温度より低温である表1に示す工程(a)の熱処理温度(1200℃)で熱処理して第2のカーボンナノファイバー(SA)を得て、第2のカーボンナノファイバー(SA)を大阪ケミカル社製回転式粉砕機ワンダーブレンダーWB−1(ステンレス粉砕刃、周速度180m/s)に入れ、表1に示す工程(b)の粉砕処理を0.5分間行って第3のカーボンナノファイバー(SAH)を得て、第3のカーボンナノファイバー(SAH)を大気雰囲気の加熱炉に入れ、表1に示す工程(c)の熱処理温度(650℃)と熱処理時間(2時間)で加熱炉内で保持して熱処理することで酸化処理を行って得た。なお、第4のカーボンナノファイバーの製造における工程(b)の粉砕処理は、前記粉砕処理カーボンナノファイバー(SH)の製造条件と同様であり、第4のカーボンナノファイバーの製造における工程(c)の酸化処理は、前記酸化処理カーボンナノファイバー(SO)の製造条件と同様であったのでここでの説明は省略する。
(1−4)このようにして得られた各カーボンナノファイバー(S,SH,SO,SAPO,SAHO)について、嵩密度、繊維長、欠陥の割合、質量残量率、ラマンピーク比、タップ密度、窒素吸着比表面積、酸素濃度、酸素濃度の増加量及び酸素濃度の増加割合を測定し、その結果を表1に示した。表1において、測定していない欄は「−」で示した。
嵩密度の測定は、零タップ密度とも呼ばれることがあり、JIS−K6219−2に従って測定した。
繊維長の測定及び欠陥を有する割合の測定は、カーボンナノファイバーを走査型電子顕微鏡(SEM)で5000倍にて40視野本撮影し、視野毎に50本ずつ合計200本の繊維について、繊維長及び欠陥を有する繊維の本数を計測して求めた。欠陥は、分岐部と折曲部を有する繊維の本数をそれぞれ数え、欠陥(分岐部と折曲部)の割合は、各欠陥を有する繊維の本数が200本中に含まれる割合(%)を計算した。また、最大繊維長が20μm以上あるカーボンナノファイバーの割合(表1には「20μm以上の割合」と示した)を計算した。
第4のカーボンナノファイバー(SAPO)の質量残量率の測定は、第3のカーボンナノファイバー(SAP)の質量を100質量%としたときにおける第4のカーボンナノファイバー(SAPO)の質量の割合を質量残量率とした。第4のカーボンナノファイバー(SAHO)の質量残量率の測定は、第3のカーボンナノファイバー(SAH)の質量を100質量%としたときにおける第4のカーボンナノファイバー(SAHO)の質量の割合を質量残量率とした。また、酸化処理カーボンナノファイバー(SO)の質量残量率の測定は、黒鉛化カーボンナノファイバー(S)の質量を100質量%としたときにおける酸化処理カーボンナノファイバー(SO)の質量の割合を質量残量率とした。
ラマンピーク比の測定は、KAISER OPTICAL SYSTEM社製HOLOLAB−5000型(532nmND:YAG)を用いてラマン散乱分光法によって各カーボンナノファイバーにおける1600cm−1付近のピーク強度Gに対する1300cm−1付近のピーク強度Dの比(D/G)を測定した。
窒素吸着比表面積の測定は、ユアサアイオニクス社製NOVA3000型(窒素ガス)を用いて各カーボンナノファイバーの窒素吸着比表面積(m/g)を測定した。表には記載していないが、第3のカーボンナノファイバー(SAH)の窒素吸着比表面積は、38(m/g)であった。
酸素濃度の測定は、第3のカーボンナノファイバー(SAPもしくはSAH)、黒鉛化カーボンナノファイバー(S)、酸化処理カーボンナノファイバー(SO)及び第4のカーボンナノファイバー(SAPOもしくはSAHO)をXPS(X線光電子分光分析法(X−ray Photoelectron Spectroscopy))を用いて測定した。具体的には、例えば第4のカーボンナノファイバーについて説明すると、まず、第4のカーボンナノファイバーを金属台上のカーボンテープ上にふりかけてカーボンテープに付着させ、カーボンテープに付着しなかった余分な第4のカーボンナノファイバーを振り落として取り除いて、金属台をXPS装置の中に装着した。XPS装置は、日本電子社製の「マイクロ分析用X線光電子分光装置JPS−9200(以下、XPS装置)を用いた。そして、次に、粉体状の試料である第4のカーボンナノファイバーをアルゴンガス濃度8×10−2Pa、0.5分間でアルゴンガスエッチングを行い、第4のカーボンナノファイバーの清浄な表面を出した。さらに、XPS装置のX線源を分析径1mm、対陰極Al/Mgツインターゲット、加速電圧10kV、エミッション電流30mAに設定して第4のカーボンナノファイバーの表面の酸素濃度を測定した。XPSによって検出された第4のカーボンナノファイバーの表面の元素は酸素と炭素であった。他のカーボンナノファイバーについても同様に測定を行った。
各カーボンナノファイバーの表面の酸素濃度の測定結果に基づいて、酸化処理を行う前の第3のカーボンナノファイバー(SAP)の表面酸素濃度(a)に対する第4のカーボンナノファイバー(SAPO)の表面酸素濃度(b)の増加量(c=b−a)及び表面酸素濃度の増加割合(d=100・c/a)を計算し、表1に示した。また、酸化処理を行う前の第3のカーボンナノファイバー(SAH)の表面酸素濃度(a)に対する第4のカーボンナノファイバー(SAHO)の表面酸素濃度(b)の増加量(c=b−a)及び表面酸素濃度の増加割合(d=100・c/a)を計算し、表1に示した。また、酸化処理を行う前の黒鉛化処理カーボンナノファイバー(S)の表面酸素濃度(a)に対する酸化処理カーボンナノファイバー(SO)の表面酸素濃度(b)の増加量(c=b−a)及び表面酸素濃度の増加割合(d=100・c/a)を計算し、表1に示した。
(1-3) The fourth carbon nanofiber (shown as “SAPO” in the table) using the compression treatment in step (b) is the first carbon nanofiber obtained in (1-1), A second carbon nanofiber (SA) is obtained by heat treatment at a heat treatment temperature (1200 ° C.) of step (a) shown in Table 1 which is lower than the reaction temperature in the vapor phase growth method in an inert gas atmosphere, The second carbon nanofiber (SA) is put into a dry compression granulator having two rolls and the roll treatment in the step (b) shown in Table 1 is performed to obtain a third carbon nanofiber (SAP). Then, the third carbon nanofiber (SAP) is put in a heating furnace in an air atmosphere, and is held in the heating furnace at a heat treatment temperature (650 ° C.) and a heat treatment time (2 hours) in step (c) shown in Table 1. Oxidation treatment by heat treatment Give me. In addition, the roll process of the process (b) in manufacture of a 4th carbon nanofiber was obtained by throwing the 2nd carbon nanofiber (SA) into the dry compression granulator which has two rolls. The dry compression granulator is a roll press (roll diameter is 150 mm, roll is smooth roll, roll interval is 0 mm, set compression force between rolls (linear pressure) is 1960 N / cm, gear ratio is 1: 1.3, roll rotation Several rpm). The roll-treated carbon nanofiber was granulated into a plate-like lump (carbon nanofiber aggregate) having a diameter of about 2 to 3 cm. The granulated plate-like lump was further crushed through a crushing and granulating machine (rotation speed: 15 rpm, screen: 5 mm) having eight rotary blades to adjust the particle size. In addition, since the oxidation treatment in the step (c) in the production of the fourth carbon nanofiber was the same as the production conditions of the oxidation treatment carbon nanofiber (SO), description thereof is omitted here.
The fourth carbon nanofiber (shown as “SAHO” in the table) using the pulverization treatment in step (b) is the same as the first carbon nanofiber obtained in (1-1) above in an inert gas atmosphere. The second carbon nanofiber (SA) is obtained by heat treatment at the heat treatment temperature (1200 ° C.) of step (a) shown in Table 1 which is lower than the reaction temperature in the vapor phase growth method. The fiber (SA) was put into a rotary pulverizer wonder blender WB-1 (stainless steel pulverizing blade, peripheral speed 180 m / s) manufactured by Osaka Chemical Co. A third carbon nanofiber (SAH) is obtained, and the third carbon nanofiber (SAH) is placed in a heating furnace in an air atmosphere, and the heat treatment temperature (650 ° C.) and heat treatment time in step (c) shown in Table 1 Held in a heating furnace obtained by performing an oxidation process by heat treatment for 2 hours). In addition, the grinding process of the process (b) in manufacture of a 4th carbon nanofiber is the same as the manufacturing conditions of the said grinding | pulverization process carbon nanofiber (SH), and the process (c) in manufacture of a 4th carbon nanofiber. Since the oxidation treatment was the same as the production conditions for the oxidation-treated carbon nanofiber (SO), description thereof is omitted here.
(1-4) For each carbon nanofiber (S, SH, SO, SAPO, SAHO) thus obtained, the bulk density, fiber length, defect ratio, mass residual ratio, Raman peak ratio, tap density The nitrogen adsorption specific surface area, the oxygen concentration, the amount of increase in oxygen concentration and the rate of increase in oxygen concentration were measured, and the results are shown in Table 1. In Table 1, unmeasured columns are indicated by “−”.
The measurement of the bulk density is sometimes called a zero tap density, and was measured according to JIS-K6219-2.
The measurement of the fiber length and the ratio of having defects are performed by taking 40 field images of carbon nanofibers at a magnification of 5000 with a scanning electron microscope (SEM), and 50 fiber lengths for a total of 200 fibers for each field of view. And the number of fibers having defects was determined by measurement. Defects count the number of fibers having branched portions and bent portions, respectively, and the ratio of defects (branched portions and bent portions) is the ratio (%) that the number of fibers having each defect is included in 200. Calculated. The ratio of carbon nanofibers having a maximum fiber length of 20 μm or more (shown as “a ratio of 20 μm or more” in Table 1) was calculated.
The measurement of the remaining mass ratio of the fourth carbon nanofiber (SAPO) is the ratio of the mass of the fourth carbon nanofiber (SAPO) when the mass of the third carbon nanofiber (SAP) is 100 mass%. Was defined as the remaining mass rate. The measurement of the remaining mass ratio of the fourth carbon nanofiber (SAHO) is the ratio of the mass of the fourth carbon nanofiber (SAHO) when the mass of the third carbon nanofiber (SAH) is 100 mass%. Was defined as the remaining mass rate. Moreover, the measurement of the residual mass ratio of oxidized carbon nanofibers (SO) is based on the ratio of the mass of oxidized carbon nanofibers (SO) when the mass of graphitized carbon nanofibers (S) is 100% by mass. The residual mass rate was assumed.
Measurement of the Raman peak ratio, KAISER OPTICAL SYSTEM Co. HOLOLAB-5000 Type: peak intensity at around 1300 cm -1 by Raman scattering spectroscopy using a (532nmND YAG) to the peak intensity G in the vicinity of 1600 cm -1 in each carbon nanofiber The ratio of D (D / G) was measured.
The nitrogen adsorption specific surface area was measured by measuring the nitrogen adsorption specific surface area (m 2 / g) of each carbon nanofiber using NOVA3000 type (nitrogen gas) manufactured by Yuasa Ionics. Although not shown in the table, the nitrogen adsorption specific surface area of the third carbon nanofiber (SAH) was 38 (m 2 / g).
The measurement of the oxygen concentration was performed using XPS (third carbon nanofiber (SAP or SAH), graphitized carbon nanofiber (S), oxidized carbon nanofiber (SO) and fourth carbon nanofiber (SAPO or SAHO). It measured using the X-ray photoelectron spectroscopy (X-ray Photoelectron Spectroscopy). Specifically, for example, the fourth carbon nanofiber will be described. First, the fourth carbon nanofiber is sprinkled on the carbon tape on the metal base to adhere to the carbon tape, and the extra carbon nanofiber that has not adhered to the carbon tape is first attached. The fourth carbon nanofiber was shaken off and a metal base was mounted in the XPS apparatus. As the XPS apparatus, “X-ray photoelectron spectrometer JPS-9200 for micro analysis (hereinafter referred to as XPS apparatus) manufactured by JEOL Ltd. was used. Next, a fourth carbon nanofiber as a powder sample was used. Argon gas etching was performed at an argon gas concentration of 8 × 10 −2 Pa for 0.5 minutes to bring out a clean surface of the fourth carbon nanofiber, and the X-ray source of the XPS apparatus had an analysis diameter of 1 mm and a counter cathode. The oxygen concentration on the surface of the fourth carbon nanofiber was measured by setting an Al / Mg twin target, an acceleration voltage of 10 kV, and an emission current of 30 mA.The elements on the surface of the fourth carbon nanofiber detected by XPS were oxygen and The same measurement was performed on other carbon nanofibers.
Based on the measurement result of the oxygen concentration on the surface of each carbon nanofiber, the fourth carbon nanofiber (SAPO) of the fourth carbon nanofiber (SAPO) with respect to the surface oxygen concentration ( ap ) of the third carbon nanofiber (SAP) before the oxidation treatment is performed. The amount of increase in surface oxygen concentration (b p ) (c p = b p −a p ) and the rate of increase in surface oxygen concentration (d p = 100 · c p / a p ) were calculated and are shown in Table 1. Further, the amount of increase in the surface oxygen concentration (b h ) of the fourth carbon nanofiber (SAHO) relative to the surface oxygen concentration (a h ) of the third carbon nanofiber (SAH) before the oxidation treatment (c h = b h −a h ) and the rate of increase of the surface oxygen concentration (d h = 100 · c h / a h ) were calculated and shown in Table 1. Further, the amount of increase in the surface oxygen concentration (b S ) of the oxidized carbon nanofiber (SO) relative to the surface oxygen concentration (a S ) of the graphitized carbon nanofiber (S) before the oxidation treatment (c S = b S- a S ) and the rate of increase in surface oxygen concentration (d S = 100 · c S / a S ) were calculated and are shown in Table 1.

Figure JPOXMLDOC01-appb-T000001
Figure JPOXMLDOC01-appb-T000001

 (2)実施例1~8及び比較例1~9の炭素繊維複合材料サンプルの作製
(2−1)実施例1~2及び比較例1~5サンプルとして、ロール径が6インチのオープンロール(ロール温度10~20℃)に、表2,3に示す100質量部(phr)の含フッ素エラストマー(「FKM」)を投入して、ロールに巻き付かせた。次に、表2,3に示す質量部(phr)の前記(1)で得られた各カーボンナノファイバーを、トリアリルイソシアネート、パーオキサイド等の配合剤と共にエラストマーに投入した。このとき、ロール間隙を1.5mmとした。配合剤を投入し終わったら、配合剤を含む混合物をロールから取り出した。ロール間隙を1.5mmから0.3mmと狭くして、さらに混合物をロールに投入して薄通しをした。このとき、2本のロールの表面速度比を1.1とした。薄通しは繰り返し10回行った。ロールを所定の間隙(1.1mm)にセットして、薄通しした複合材料を投入し、分出しして無架橋体の炭素繊維複合材料を得た。このようにして得られた炭素繊維複合材料をロールで圧延後、170℃、10分間プレス成形(キュア)した後、さらに200℃、24時間ポストキュアして、実施例1~2及び比較例1~5の架橋体の炭素繊維複合材料(厚さ1mmのシート形状)を得た。なお、表2,4における「FKM」がデュポン・ダウ・エラストマー・ジャパン社製の3元系の含フッ素エラストマーのバイトンGF−600S(重量平均分子量50,000、T2n/30℃が50μ秒)であった。
(2) Production of carbon fiber composite material samples of Examples 1 to 8 and Comparative Examples 1 to 9 (2-1) Examples of Examples 1 to 2 and Comparative Examples 1 to 5 are open rolls having a roll diameter of 6 inches ( 100 parts by mass (phr) of a fluorine-containing elastomer (“FKM”) shown in Tables 2 and 3 was added to a roll temperature of 10 to 20 ° C. and wound around a roll. Next, each carbon nanofiber obtained in (1) in parts by mass (phr) shown in Tables 2 and 3 was added to the elastomer together with compounding agents such as triallyl isocyanate and peroxide. At this time, the roll gap was set to 1.5 mm. When the compounding agent was charged, the mixture containing the compounding agent was taken out from the roll. The roll gap was narrowed from 1.5 mm to 0.3 mm, and the mixture was further introduced into the roll for thinning. At this time, the surface speed ratio of the two rolls was set to 1.1. Thinning was repeated 10 times. A roll was set in a predetermined gap (1.1 mm), a thin composite material was charged, and dispensed to obtain a non-crosslinked carbon fiber composite material. The carbon fiber composite material thus obtained was rolled with a roll, press-molded (cured) at 170 ° C. for 10 minutes, and further post-cured at 200 ° C. for 24 hours. Examples 1-2 and Comparative Example 1 A crosslinked carbon fiber composite material (sheet shape having a thickness of 1 mm) was obtained. “FKM” in Tables 2 and 4 is Viton GF-600S (a weight average molecular weight of 50,000, T2n / 30 ° C. is 50 μsec), a ternary fluorine-containing elastomer manufactured by DuPont Dow Elastomer Japan. there were.

(2−2)実施例3~8及び比較例6~9サンプルとして、オープンロール(ロール設定温度20℃)に、表2、3,5に示す所定量のEPDM(エチレン−プロピレンゴム)を投入し素練り後、(1)で得られた各カーボンナノファイバーをエラストマーに投入し混練りの後、第1の混練工程を行いロールから取り出した。さらに、その混合物をロール温度100℃に設定されたオープンロールに再度投入し、第2の混練工程を行って取り出した。次に、この混合物をオープンロール(ロール温度10~20℃、ロール間隔0.3mm)に巻きつけ、薄通しを繰り返し5回行なった。このとき、2本のロールの表面速度比を1.1とした。さらに、ロール間隙を1.1mmにセットして、薄通しして得られた炭素繊維複合材料を投入し、分出しした。分出ししたシートを90℃、5分間圧縮成形して厚さ1mmの実施例3~8及び比較例6~9の無架橋体の炭素繊維複合材料サンプルを得た。さらに、薄通しして得られた無架橋の炭素繊維複合材料にパーオキサイド2質量部(phr)を混合し、ロール間隙を1.1mmにセットしたオープンロールに投入し、分出しした。分出しして金型サイズに切り取ったパーオキサイドを含む炭素繊維複合材料を金型にセットし、175℃、100kgf/cm、20分間圧縮成形して厚さ1mmの実施例3~5及び比較例6~8の架橋体の炭素繊維複合材料サンプルを得た。なお、表2、3、5において、「EPDM」はJSR社製のエチレン−プロピレンゴムの商品名EP103AFであった。また、比較例1、6は、カーボンナノファイバーを配合しなかったが、同様の混練工程を行った。 (2-2) As examples 3 to 8 and comparative examples 6 to 9, a predetermined amount of EPDM (ethylene-propylene rubber) shown in Tables 2, 3 and 5 was put into an open roll (roll set temperature 20 ° C.). After kneading, each carbon nanofiber obtained in (1) was put into an elastomer and kneaded, and then the first kneading step was performed and taken out from the roll. Further, the mixture was again put into an open roll set at a roll temperature of 100 ° C., and taken out by performing a second kneading step. Next, this mixture was wound around an open roll (roll temperature: 10 to 20 ° C., roll interval: 0.3 mm), and thinning was repeated 5 times. At this time, the surface speed ratio of the two rolls was set to 1.1. Furthermore, the carbon fiber composite material obtained by setting the roll gap to 1.1 mm and passing through was put and dispensed. The separated sheets were compression molded at 90 ° C. for 5 minutes to obtain uncrosslinked carbon fiber composite material samples of Examples 3 to 8 and Comparative Examples 6 to 9 having a thickness of 1 mm. Further, 2 parts by mass of peroxide (phr) was mixed with the non-crosslinked carbon fiber composite material obtained through thinning, and the mixture was put into an open roll having a roll gap set to 1.1 mm and dispensed. Carbon fiber composite material containing peroxide that was dispensed and cut into a mold size was set in a mold, compression molded at 175 ° C., 100 kgf / cm 2 for 20 minutes, and Examples 3 to 5 having a thickness of 1 mm and comparison The crosslinked carbon fiber composite material samples of Examples 6 to 8 were obtained. In Tables 2, 3, and 5, “EPDM” was the trade name EP103AF of ethylene-propylene rubber manufactured by JSR. In Comparative Examples 1 and 6, carbon nanofibers were not blended, but the same kneading process was performed.

 (3)パルス法NMRを用いた測定
実施例1~8及び比較例1~9の各無架橋体の炭素繊維複合材料サンプルについて、パルス法NMRを用いてハーンエコー法による測定を行った。この測定は、日本電子(株)製「JMN−MU25」を用いて行った。測定は、観測核がH、共鳴周波数が25MHz、90°パルス幅が2μsecの条件で行い、ハーンエコー法のパルスシーケンス(90°x−Pi−180°x)にて、Piをいろいろ変えて減衰曲線を測定した。また、サンプルは、磁場の適正範囲までサンプル管に挿入して測定した。測定温度は、150℃であった。この測定によって、各サンプルについて第1のスピン−スピン緩和時間(T2n/150℃)と第2のスピン−スピン緩和時間を有する成分の成分分率(fnn)とを求めた。測定結果を表2~4に示した。なお、同様に測定した原料ゴムの第1のスピン−スピン緩和時間(T2n/30℃)も表2~5に示した。なお、実施例1~5,7,8の炭素繊維複合材料サンプルについては、カーボンナノファイバーによる磁場をみだす影響があり、測定ができなかった。
(3) Measurement using pulsed NMR The uncrosslinked carbon fiber composite material samples of Examples 1 to 8 and Comparative Examples 1 to 9 were measured by the Hahn echo method using pulsed NMR. This measurement was performed using “JMN-MU25” manufactured by JEOL Ltd. The measurement is performed under the condition that the observation nucleus is 1 H, the resonance frequency is 25 MHz, the 90 ° pulse width is 2 μsec, and Pi is changed in various ways by the pulse sequence of the Hahn echo method (90 ° x-Pi-180 ° x). The decay curve was measured. Further, the sample was measured by inserting it into a sample tube up to an appropriate range of the magnetic field. The measurement temperature was 150 ° C. By this measurement, the first spin-spin relaxation time (T2n / 150 ° C.) and the component fraction (fnn) of the component having the second spin-spin relaxation time were determined for each sample. The measurement results are shown in Tables 2-4. The first spin-spin relaxation times (T2n / 30 ° C.) of the raw rubber measured in the same manner are also shown in Tables 2 to 5. Note that the carbon fiber composite material samples of Examples 1 to 5, 7, and 8 were affected by the magnetic field generated by the carbon nanofibers and could not be measured.

 (4)硬度(Hs)、100%モジュラス(M100)、引張強さ(TB)、破断伸び(EB)、動的弾性率(E’)及び体積固有抵抗値の測定
実施例1~8及び比較例1~9の架橋体の炭素繊維複合材料サンプルについて、ゴム硬度(Hs(JIS−A))をJIS K 6253に基づいて測定した。
実施例1~8及び比較例1~9の架橋体の炭素繊維複合材料サンプルをJIS6号形のダンベル形状に切り出した試験片について、東洋精機社製の引張試験機を用いて、23±2℃、引張速度500mm/minでJIS K6251に基づいて引張試験を行い引張強さ(TB(MPa))、破断伸び(EB(%))及び100%応力(M100)を測定した。
実施例1~8及び比較例1~9の架橋体の炭素繊維複合材料サンプルを短冊形(40×1×5(巾)mm)に切り出した試験片について、SII社製の動的粘弾性試験機DMS6100を用いて、チャック間距離20mm、測定温度−100~300℃、動的ひずみ±0.05%、周波数10HzでJIS K6394に基づいて動的粘弾性試験を行い測定温度が30℃及び200℃における動的弾性率(E’、単位はMPa)を測定した。
実施例1~8及び比較例1~9の架橋体の炭素繊維複合材料サンプル(幅50mm×長さ50mm×厚さ1mm)をJIS K 6271に基づいて、23℃における体積固有抵抗値(Ω・cm)を測定した。その測定結果に基づいて、炭素繊維複合材料サンプルの電気絶縁性を評価し、体積固有抵抗値が1×10以上であれば絶縁性が良好(表では「○」と示す)とし、体積固有抵抗値が1×10未満であれば絶縁性が低い(表では「×」と示す)とした。
(4) Measurement of Hardness (Hs), 100% Modulus (M100), Tensile Strength (TB), Elongation at Break (EB), Dynamic Elastic Modulus (E ′) and Volume Specific Resistance Examples 1 to 8 and Comparison For the crosslinked carbon fiber composite material samples of Examples 1 to 9, rubber hardness (Hs (JIS-A)) was measured based on JIS K 6253.
About the test piece which cut the carbon fiber composite material sample of the bridge | crosslinking body of Examples 1-8 and Comparative Examples 1-9 into the dumbbell shape of JIS6 type, it was 23 +/- 2 degreeC using the tensile tester by Toyo Seiki Co., Ltd. Then, a tensile test was performed based on JIS K6251 at a tensile speed of 500 mm / min, and tensile strength (TB (MPa)), elongation at break (EB (%)) and 100% stress (M100) were measured.
A dynamic viscoelasticity test made by SII Co., Ltd. was performed on test pieces obtained by cutting the carbon fiber composite material samples of the crosslinked bodies of Examples 1 to 8 and Comparative Examples 1 to 9 into strips (40 × 1 × 5 (width) mm). Using a machine DMS6100, a distance between chucks of 20 mm, a measurement temperature of −100 to 300 ° C., a dynamic strain of ± 0.05%, and a frequency of 10 Hz were subjected to a dynamic viscoelasticity test based on JIS K6394, and the measurement temperatures were 30 ° C. and 200 ° C. The dynamic elastic modulus at E ° C. (E ′, unit is MPa) was measured.
Samples of carbon fiber composite materials (width 50 mm × length 50 mm × thickness 1 mm) of the crosslinked bodies of Examples 1 to 8 and Comparative Examples 1 to 9 were measured based on JIS K 6271 at a volume specific resistance value (Ω · cm). Based on the measurement results, the electrical insulation of the carbon fiber composite material sample is evaluated. If the volume resistivity is 1 × 10 6 or more, the insulation is good (shown as “◯” in the table), and the volume is specific. If the resistance value is less than 1 × 10 6 , the insulation is low (shown as “x” in the table).

Figure JPOXMLDOC01-appb-T000002
Figure JPOXMLDOC01-appb-T000002

Figure JPOXMLDOC01-appb-T000003
Figure JPOXMLDOC01-appb-T000003

Figure JPOXMLDOC01-appb-T000004
Figure JPOXMLDOC01-appb-T000004

Figure JPOXMLDOC01-appb-T000005
Figure JPOXMLDOC01-appb-T000005

 表2~5の結果からも明らかなように、実施例1~2の第4のカーボンナノファイバーを配合した架橋体の炭素繊維複合材料は、比較例1~5の炭素繊維複合材料に比べて、第4のカーボンナノファイバーを大量に配合しても体積固有抵抗値が高く、電気絶縁性が良好であった。また、実施例3~8の第4のカーボンナノファイバーを配合した架橋体の炭素繊維複合材料は、比較例6~9の炭素繊維複合材料に比べて、第4のカーボンナノファイバーを大量に配合しても体積固有抵抗値が高く、電気絶縁性が良好であった。 As is apparent from the results in Tables 2 to 5, the crosslinked carbon fiber composite material containing the fourth carbon nanofibers of Examples 1 and 2 is more in comparison with the carbon fiber composite materials of Comparative Examples 1 to 5. Even when a large amount of the fourth carbon nanofiber was blended, the volume resistivity was high and the electrical insulation was good. In addition, the crosslinked carbon fiber composite material containing the fourth carbon nanofibers of Examples 3 to 8 contains a larger amount of the fourth carbon nanofiber than the carbon fiber composite materials of Comparative Examples 6 to 9. Even so, the volume resistivity was high and the electrical insulation was good.

2  オープンロール
10 第1のロール
20 第2のロール
30 エラストマー
60 第2のカーボンナノファイバー
62 折曲部
64 分岐部
70 乾式圧縮造粒機
72 第1のロール
74 第2のロール
80 第3のカーボンナノファイバー
90 第4のカーボンナノファイバー
150 プラットホーム
160 ダウンホール装置
161 筐体
162 電気コネクタ
163 電線
164 ケーブル
165 コイル
166 電気基板
167 電子部品
168 センサ
2 Open roll 10 1st roll 20 2nd roll 30 Elastomer 60 2nd carbon nanofiber 62 Bending part 64 Branching part 70 Dry compression granulator 72 1st roll 74 2nd roll 80 3rd carbon Nanofiber 90 Fourth carbon nanofiber 150 Platform 160 Downhole device 161 Housing 162 Electric connector 163 Electric wire 164 Cable 165 Coil 166 Electric substrate 167 Electronic component 168 Sensor

Claims (28)

 エラストマー100質量部に対して、分岐部を減らしかつ酸化したカーボンナノファイバーを20質量部~100質量部含み、
 200℃、10Hzにおける動的弾性率(E’)が10MPa~1000MPaであって、
 体積固有抵抗値が10Ω・cm~1018Ω・cmである、炭素繊維複合材料。
20 parts by mass to 100 parts by mass of carbon nanofibers with reduced branch parts and oxidized with respect to 100 parts by mass of the elastomer,
The dynamic elastic modulus (E ′) at 200 ° C. and 10 Hz is 10 MPa to 1000 MPa,
A carbon fiber composite material having a volume resistivity of 10 6 Ω · cm to 10 18 Ω · cm.
 請求項1において、
 前記カーボンナノファイバーは、前記エラストマーに配合される前に、機械的作用により分岐部を減らした、炭素繊維複合材料。
In claim 1,
The carbon nanofiber is a carbon fiber composite material in which branch portions are reduced by a mechanical action before being blended with the elastomer.
 請求項2において、
 前記機械的作用は、圧縮処理によってなされる、炭素繊維複合材料。
In claim 2,
The mechanical action is a carbon fiber composite material made by a compression process.
 請求項3において、
 前記エラストマーが含フッ素エラストマーであって、
 200℃、10Hzにおける動的弾性率(E’)が15MPa~300MPaであって、
 体積固有抵抗値が1011Ω・cm~1018Ω・cmである、炭素繊維複合材料。
In claim 3,
The elastomer is a fluorine-containing elastomer,
The dynamic elastic modulus (E ′) at 200 ° C. and 10 Hz is 15 MPa to 300 MPa,
A carbon fiber composite material having a volume resistivity of 10 11 Ω · cm to 10 18 Ω · cm.
 請求項3において、
 前記エラストマーがエチレン−プロピレンゴムであって、
 200℃、10Hzにおける動的弾性率(E’)が10MPa~200MPaであって、
 体積固有抵抗値が10Ω・cm~1018Ω・cmである、炭素繊維複合材料。
In claim 3,
The elastomer is ethylene-propylene rubber,
The dynamic elastic modulus (E ′) at 200 ° C. and 10 Hz is 10 MPa to 200 MPa,
A carbon fiber composite material having a volume resistivity of 10 7 Ω · cm to 10 18 Ω · cm.
 請求項2において、
 前記機械的作用は、粉砕処理によってなされる、炭素繊維複合材料。
In claim 2,
The mechanical action is a carbon fiber composite material made by a pulverization process.
 請求項6において、
 前記エラストマーがエチレン−プロピレンゴムであって、
 200℃、10Hzにおける動的弾性率(E’)が10MPa~200MPaであって、
 体積固有抵抗値が10Ω・cm~1018Ω・cmである、炭素繊維複合材料。
In claim 6,
The elastomer is ethylene-propylene rubber,
The dynamic elastic modulus (E ′) at 200 ° C. and 10 Hz is 10 MPa to 200 MPa,
A carbon fiber composite material having a volume resistivity of 10 8 Ω · cm to 10 18 Ω · cm.
 請求項1~7のいずれかにおいて、
 前記カーボンナノファイバーは、最大繊維長が20μm未満である、炭素繊維複合材料。
In any one of Claims 1-7,
The carbon nanofiber is a carbon fiber composite material having a maximum fiber length of less than 20 μm.
 請求項1~8のいずれかに記載の炭素繊維複合材料を含む、油田用途の絶縁性物品。 An insulating article for use in oil fields, comprising the carbon fiber composite material according to any one of claims 1 to 8.  請求項9に記載の絶縁性物品を含む、電子部品。 Electronic parts including the insulating article according to claim 9.  筐体と、該筐体内に配置された請求項10に記載の電子部品と、を備える、検層装置。 A logging apparatus comprising a housing and the electronic component according to claim 10 disposed in the housing.  気相成長法によって製造された第1のカーボンナノファイバーを、前記気相成長法における反応温度より高温であって、かつ、1100℃~1600℃で熱処理して第2のカーボンナノファイバーを得る工程(a)と、
 前記第2のカーボンナノファイバーを機械的作用によって処理して、第2のカーボンナノファイバーの分岐部を減らして、第3のカーボンナノファイバーを得る工程(b)と、
 前記第3のカーボンナノファイバーを酸素を含有する雰囲気中で600℃~800℃で熱処理して、酸化した第4のカーボンナノファイバーを得る工程(c)と、
 前記第4のカーボンナノファイバーを、エラストマーに混合し、剪断力で該エラストマー中に均一に分散して炭素繊維複合材料を得る工程(d)と、
 を含む、炭素繊維複合材料の製造方法。
A step of obtaining a second carbon nanofiber by heat-treating the first carbon nanofiber produced by the vapor deposition method at a temperature higher than the reaction temperature in the vapor deposition method at 1100 ° C. to 1600 ° C. (A) and
Treating the second carbon nanofibers by a mechanical action to reduce the branching portions of the second carbon nanofibers to obtain third carbon nanofibers;
(C) a step of heat-treating the third carbon nanofibers in an atmosphere containing oxygen at 600 ° C. to 800 ° C. to obtain oxidized fourth carbon nanofibers;
A step (d) of mixing the fourth carbon nanofibers with an elastomer and uniformly dispersing in the elastomer with a shearing force to obtain a carbon fiber composite material;
A method for producing a carbon fiber composite material, comprising:
 請求項12において、
 前記工程(a)の前記熱処理は、1200℃~1500℃である、炭素繊維複合材料の製造方法。
In claim 12,
The method for producing a carbon fiber composite material, wherein the heat treatment in the step (a) is 1200 ° C to 1500 ° C.
 請求項12または13において、
 前記工程(b)で得られた前記第3のカーボンナノファイバーは、最大繊維長が20μm未満である、炭素繊維複合材料の製造方法。
In claim 12 or 13,
The third carbon nanofiber obtained in the step (b) has a maximum fiber length of less than 20 μm, and is a method for producing a carbon fiber composite material.
 請求項12~14のいずれかにおいて、
 前記工程(b)の前記機械的作用は、圧縮処理によってなされ、
 前記圧縮処理によって得られた第3のカーボンナノファイバーは、分岐部を有しない、炭素繊維複合材料の製造方法。
In any one of claims 12 to 14,
The mechanical action of the step (b) is performed by a compression process,
The 3rd carbon nanofiber obtained by the said compression process is a manufacturing method of a carbon fiber composite material which does not have a branch part.
 請求項15において、
 前記圧縮処理は、少なくとも2本の回転するロール間に前記第2のカーボンナノファイバーを投入して、前記第2のカーボンナノファイバーに剪断力と圧縮力とを加えることによって行われる、炭素繊維複合材料の製造方法。
In claim 15,
The compression treatment is performed by putting the second carbon nanofiber between at least two rotating rolls and applying a shearing force and a compression force to the second carbon nanofiber. Material manufacturing method.
 請求項15または16において、
 前記圧縮処理は、カーボンナノファイバー同士を結合するためのバインダーを用いない、炭素繊維複合材料の製造方法。
In claim 15 or 16,
The said compression process is a manufacturing method of a carbon fiber composite material which does not use the binder for couple | bonding carbon nanofibers.
 請求項15~17のいずれかにおいて、
 前記圧縮処理は、乾式圧縮造粒機で行われる、炭素繊維複合材料の製造方法。
In any one of claims 15 to 17,
The said compression process is a manufacturing method of a carbon fiber composite material performed with a dry compression granulator.
 請求項12~14のいずれかにおいて、
 前記工程(b)の前記機械的作用は、粉砕処理によってなされ、
 前記第3のカーボンナノファイバーのタップ密度は、前記第2のカーボンナノファイバーのタップ密度の1.5倍~10倍である、炭素繊維複合材料の製造方法。
In any one of claims 12 to 14,
The mechanical action of the step (b) is performed by a pulverization process,
The method for producing a carbon fiber composite material, wherein the tap density of the third carbon nanofiber is 1.5 to 10 times the tap density of the second carbon nanofiber.
 請求項19において、
 前記粉砕処理は、前記第2のカーボンナノファイバーの窒素吸着比表面積の1.1倍~5.0倍の窒素吸着比表面積を有する前記第3のカーボンナノファイバーを得る、炭素繊維複合材料の製造方法。
In claim 19,
The pulverization treatment produces the third carbon nanofiber having a nitrogen adsorption specific surface area that is 1.1 to 5.0 times the nitrogen adsorption specific surface area of the second carbon nanofiber. Method.
 請求項19または20において、
 前記粉砕処理は、衝撃及び/または剪断力を利用した乾式粉砕で行なう、炭素繊維複合材料の製造方法。
In claim 19 or 20,
The method for producing a carbon fiber composite material, wherein the pulverization is performed by dry pulverization using impact and / or shear force.
 請求項12~21のいずれかにおいて、
 X線光電子分光法(XPS)で測定した、前記第3のカーボンナノファイバーの表面の酸素濃度に対する前記第4のカーボンナノファイバーの表面の酸素濃度の増加量は、0.5atm%~2.6atm%である、炭素繊維複合材料の製造方法。
In any one of claims 12 to 21
The amount of increase in the oxygen concentration on the surface of the fourth carbon nanofiber relative to the oxygen concentration on the surface of the third carbon nanofiber measured by X-ray photoelectron spectroscopy (XPS) is 0.5 atm% to 2.6 atm. %, The method for producing a carbon fiber composite material.
 請求項12~22のいずれかにおいて、
 X線光電子分光法(XPS)で測定した、前記第3のカーボンナノファイバーの表面の酸素濃度に対する前記第4のカーボンナノファイバーの表面の酸素濃度の増加割合は、20%~120%である、炭素繊維複合材料の製造方法。
In any one of claims 12 to 22,
The increase rate of the oxygen concentration on the surface of the fourth carbon nanofiber relative to the oxygen concentration on the surface of the third carbon nanofiber measured by X-ray photoelectron spectroscopy (XPS) is 20% to 120%. A method for producing a carbon fiber composite material.
 請求項12~23のいずれかにおいて、
 前記工程(c)の熱処理は、前記第3のカーボンナノファイバーの質量を2%~20%減量して前記第4のカーボンナノファイバーを得る、炭素繊維複合材料の製造方法。
In any one of claims 12 to 23
The heat treatment in the step (c) is a method for producing a carbon fiber composite material, wherein the fourth carbon nanofibers are obtained by reducing the mass of the third carbon nanofibers by 2% to 20%.
 請求項12~24のいずれかにおいて、
 前記工程(c)で得られた前記第4のカーボンナノファイバーは、X線光電子分光法(XPS)で測定した表面の酸素濃度が2.6atm%~4.6atm%である、炭素繊維複合材料の製造方法。
In any one of claims 12 to 24,
The fourth carbon nanofiber obtained in the step (c) has a surface oxygen concentration of 2.6 atm% to 4.6 atm% measured by X-ray photoelectron spectroscopy (XPS). Manufacturing method.
 請求項12~25のいずれかにおいて、
 前記工程(c)で得られた前記第4のカーボンナノファイバーは、ラマン散乱分光法によって測定される1600cm−1付近のピーク強度Gに対する1300cm−1付近のピーク強度Dの比(D/G)が0.12~0.22である、炭素繊維複合材料の製造方法。
In any one of claims 12 to 25
The fourth carbon nanofiber obtained in the step (c) the ratio of the peak intensity D of around 1300 cm -1 to the peak intensity G of around 1600 cm -1 measured by Raman scattering spectroscopy (D / G) A method for producing a carbon fiber composite material having a thickness of 0.12 to 0.22.
 請求項12~26のいずれかにおいて、
 前記工程(c)で得られた前記第4のカーボンナノファイバーは、窒素吸着比表面積が45m/g~60m/gである、炭素繊維複合材料の製造方法。
In any one of claims 12 to 26,
The method for producing a carbon fiber composite material, wherein the fourth carbon nanofiber obtained in the step (c) has a nitrogen adsorption specific surface area of 45 m 2 / g to 60 m 2 / g.
 請求項12~26のいずれかにおいて、
 前記工程(c)で得られた前記第4のカーボンナノファイバーは、平均直径が70nm~100nmである、炭素繊維複合材料の製造方法。
In any one of claims 12 to 26,
The method for producing a carbon fiber composite material, wherein the fourth carbon nanofiber obtained in the step (c) has an average diameter of 70 nm to 100 nm.
PCT/JP2009/071907 2009-12-25 2009-12-25 Carbon-fiber composite material, process for producing same, insulation article, electronic component, and logging tool Ceased WO2011077598A1 (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013014699A (en) * 2011-07-05 2013-01-24 Nissin Kogyo Co Ltd Carbon fiber composite material, oil-field equipment and method for producing carbon fiber composite material
US9504151B2 (en) 2012-03-29 2016-11-22 Sumitomo Riko Company Limited Conductive composition and conductive film
US9771461B2 (en) 2013-10-17 2017-09-26 Nissin Kogyo Co., Ltd. Method for producing rubber composition and rubber composition
KR20190135197A (en) * 2018-05-28 2019-12-06 울산과학기술원 Aramid fiber/reduced graphene oxide/polyester composite
CN112213521A (en) * 2020-08-18 2021-01-12 中国航空制造技术研究院 A method for evaluating the hardness of the interfacial zone of fiber composite materials

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009127038A (en) * 2007-11-28 2009-06-11 Showa Denko Kk Resin composition, method for producing the same and use of the same
JP2009215403A (en) * 2008-03-10 2009-09-24 Teijin Ltd Sheet-like heat-conductive molded body
WO2009128374A1 (en) * 2008-04-16 2009-10-22 日信工業株式会社 Carbon nanofiber, method for production thereof, method for production of carbon fiber composite material using carbon nanofiber, and carbon fiber composite material

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009127038A (en) * 2007-11-28 2009-06-11 Showa Denko Kk Resin composition, method for producing the same and use of the same
JP2009215403A (en) * 2008-03-10 2009-09-24 Teijin Ltd Sheet-like heat-conductive molded body
WO2009128374A1 (en) * 2008-04-16 2009-10-22 日信工業株式会社 Carbon nanofiber, method for production thereof, method for production of carbon fiber composite material using carbon nanofiber, and carbon fiber composite material

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013014699A (en) * 2011-07-05 2013-01-24 Nissin Kogyo Co Ltd Carbon fiber composite material, oil-field equipment and method for producing carbon fiber composite material
US9504151B2 (en) 2012-03-29 2016-11-22 Sumitomo Riko Company Limited Conductive composition and conductive film
US9771461B2 (en) 2013-10-17 2017-09-26 Nissin Kogyo Co., Ltd. Method for producing rubber composition and rubber composition
US10087293B2 (en) 2013-10-17 2018-10-02 Nissin Kogyo Co., Ltd. Method for producing rubber composition and rubber composition
KR20190135197A (en) * 2018-05-28 2019-12-06 울산과학기술원 Aramid fiber/reduced graphene oxide/polyester composite
KR102087224B1 (en) 2018-05-28 2020-03-10 울산과학기술원 Aramid fiber/reduced graphene oxide/polyester composite
CN112213521A (en) * 2020-08-18 2021-01-12 中国航空制造技术研究院 A method for evaluating the hardness of the interfacial zone of fiber composite materials
CN112213521B (en) * 2020-08-18 2023-11-03 中国航空制造技术研究院 A method for evaluating the hardness of the interface zone of fiber composite materials

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