Carbon nanotube aggregates, conductive material, electrode, secondary battery, planar aggregate, laminate, filter, electromagnetic wave shield, and extreme ultraviolet pellicle

Abstract

The present invention provides carbon nanotube aggregates that have excellent conductivity in a carbon nanotube dispersion and that make it possible to obtain a carbon nanotube dispersion that has an appropriate density.　The present invention provides carbon nanotube aggregates that satisfy conditions (1) and (2) and a use for the carbon nanotube aggregates. (1) The carbon nanotube aggregates contain Na atoms, and the Na atom content is less than 200 mass ppm relative to the total mass of the carbon nanotube aggregates. (2) The elongation at break as measured by the following method is greater than 0% but no greater than 3.0%. The elongation at break is measured by preparing a dispersion that includes the carbon nanotube aggregates, pouring the dispersion onto a plate, using a tensile testing device to perform a tensile test on a measurement sample obtained by drying the dispersion by heating at 100°C, and calculating the elongation at break from the length of the measurement sample before measurement and the length of the measurement sample at a breaking point that is the point of maximum stress.

Description

Carbon nanotube aggregates, conductive materials, electrodes, secondary batteries, planar aggregates, laminates, filters, electromagnetic shielding, and pellicles for extreme ultraviolet radiation.

[0001] This disclosure relates to carbon nanotube aggregates, conductive materials, electrodes, secondary batteries, planar aggregates, laminates, filters, electromagnetic shielding, and pellicles for extreme ultraviolet applications.

[0002] Carbon nanotubes (hereinafter also referred to as "CNTs") are materials having a cylindrical structure formed by rolling up graphene sheets, which are composed of six-membered ring structures of carbon, in a single or multilayer configuration on the same axis. CNTs are broadly classified into single-walled CNTs, which are formed from a single layer of graphene sheet, and multilayered CNTs, which are formed from multiple layers of graphene sheet. CNTs exhibit excellent mechanical, electrical, and chemical properties, and these properties are expected to lead to applications in fields such as materials, catalysts, energy, and electronics. Various attempts have been proposed to further enhance the properties of CNTs.

[0003] For example, Patent Document 1 describes a carbon nanotube aggregate in which the sum of the iron and cobalt content and the sum of the sodium and potassium content relative to the total mass of the carbon nanotube aggregate are within a specific range, and the ratio of the volume resistivity under two specific pressure conditions is within a specific range, and which exhibits excellent conductivity when used as a carbon nanotube dispersion. Patent Document 2 describes a lithium-ion battery anode material in which the tensile strength of conductivity improvers such as carbon nanotubes is within a specific range, which effectively suppresses the volume expansion of the anode material.

[0004] Japanese Patent Publication No. 7556170, Japanese Unexamined Patent Publication No. 2023-542766

[0005] In some cases, when CNT aggregates are dispersed, it is required that they have excellent conductivity. Furthermore, when preparing dispersions using CNT aggregates, it is sometimes necessary to suppress the increase in shear force caused by viscosity.

[0006] This disclosure has been made in view of the above circumstances. One embodiment of this disclosure aims to solve the problem of providing a carbon nanotube aggregate that has excellent conductivity when used as a carbon nanotube dispersion and yields a carbon nanotube dispersion with appropriate viscosity. Another embodiment of this disclosure aims to solve the problem of providing a conductive material, electrode, secondary battery, and planar aggregate containing the above carbon nanotube aggregate. Another embodiment of this disclosure aims to solve the problem of providing a laminate comprising the above planar aggregate. Another embodiment of this disclosure aims to solve the problem of providing a filter, electromagnetic shield, and extreme ultraviolet pellicle using the above planar aggregate.

[0007] <1> A carbon nanotube aggregate that satisfies the following conditions (1) and (2). (1) It contains Na atoms, and the Na atom content is less than 200 ppm by mass relative to the total mass of the carbon nanotube aggregate. (2) The elongation at break measured by the following measurement method is greater than 0% and 3.0% or less. (Method for measuring elongation at break) A dispersion with a concentration of 0.20% by mass is prepared by mixing the carbon nanotube aggregate with water. The obtained dispersion is poured onto a 22 mm × 75 mm × 3 mm slide glass type silicon plate, heated at 100°C for 30 minutes to dry and obtain a measurement sample. The obtained measurement sample is fixed to the gripping part of a tensile testing device, and a tensile test is performed at a speed of 1 mm / min. The point where the stress is maximum is considered the breaking point, and the elongation at break is calculated from the length of the measurement sample at the breaking point and the length of the measurement sample before measurement. <2> The carbon nanotube aggregate described in <1> that satisfies the following condition (3). (3) The cumulative 50% particle size D50 in the volume-based particle size distribution is 1.0 μm or more and 15 μm or less. <3> A conductive material comprising the carbon nanotube aggregate described in <1> or <2>. <4> An electrode comprising an electrode active material and the conductive material described in <3>. <5> A secondary battery comprising the electrode described in <4>. <6> A planar aggregate comprising the carbon nanotube aggregate described in <1> or <2>. <7> A laminate comprising a substrate and the planar aggregate described in <6>. <8> A filter using the planar aggregate described in <6>. <9> An electromagnetic shield using the planar aggregate described in <6>. <10> An extreme ultraviolet pellicle using the planar aggregate described in <6>.

[0008] According to one embodiment of the present disclosure, a carbon nanotube aggregate is provided that exhibits excellent conductivity when used as a carbon nanotube dispersion and yields a carbon nanotube dispersion with appropriate viscosity. According to another embodiment of the present disclosure, a conductive material, an electrode, a secondary battery, and a planar aggregate containing the above-mentioned carbon nanotube aggregate are provided. According to yet another embodiment of the present disclosure, a laminate comprising the above-mentioned planar aggregate is provided. According to yet another embodiment of the present disclosure, a filter, an electromagnetic shield, and an extreme ultraviolet pellicle using the above-mentioned planar aggregate are provided.

[0009] The carbon nanotube assemblies, conductive materials, electrodes, secondary batteries, planar assemblies, laminates, filters, electromagnetic shields, and extreme ultraviolet pellicles related to this disclosure will be described in detail below. The following descriptions may be based on typical embodiments of this disclosure, but this disclosure is not limited to such embodiments and can be implemented with appropriate modifications within the scope of the purpose of this disclosure.

[0010] In this disclosure, numerical ranges indicated using "~" mean ranges that include the numbers before and after "~" as the minimum and maximum values, respectively. In numerical ranges described in stages in this disclosure, the upper or lower limit stated in one numerical range may be replaced with the upper or lower limit of another numerical range described in stages. Also, in numerical ranges described in this disclosure, the upper or lower limit stated in one numerical range may be replaced with the values ​​shown in the examples. In this disclosure, a combination of two or more preferred embodiments is a more preferred embodiment. In this disclosure, the amount of each component means the total amount of multiple substances if there are multiple substances corresponding to each component, unless otherwise specified. In this specification, the term "process" includes not only independent processes but also processes that cannot be clearly distinguished from other processes, as long as the intended purpose of the process is achieved.

[0011] In this disclosure, the terms "carbon nanotube," "single-walled carbon nanotube," "multi-walled carbon nanotube," "carbon nanotube aggregate," "carbon nanotube having a maximum length of 1,000 μm to 30,000 μm," and "carbon nanotube dispersion" may be abbreviated as "CNT," "SWCNT," "MWCNT," "CNT aggregate," "ULCNT," and "CNT dispersion," respectively.

[0012] [CNT aggregate] The CNT aggregate according to this disclosure satisfies the following conditions (1) and (2): (1) It contains Na atoms, and the Na atom content is less than 200 ppm by mass relative to the total mass of the carbon nanotube aggregate. (2) The elongation at break measured by the following measurement method is greater than 0% and 3.0% or less. (Method for measuring elongation at break) A dispersion with a concentration of 0.20% by mass is prepared by mixing the carbon nanotube aggregate with water. The obtained dispersion is poured onto a 22 mm × 75 mm × 3 mm slide glass type silicon plate, heated at 100°C for 30 minutes to dry and obtain a measurement sample. The obtained measurement sample is fixed to the gripping part of a tensile testing device, and a tensile test is performed at a speed of 1 mm / min. The point where the stress is maximum is considered the breaking point, and the elongation at break is calculated from the length of the measurement sample at the breaking point and the length of the measurement sample before measurement.

[0013] A CNT aggregate that satisfies conditions (1) and (2), i.e., the CNT aggregate according to this disclosure, is provided, which has excellent conductivity when used as a carbon nanotube dispersion and yields a carbon nanotube dispersion with appropriate viscosity. On the other hand, Patent Documents 1 and 2 do not contain any descriptions that focus on conditions (1) and (2).

[0014] Patent Document 1 does not focus on the dispersibility of carbon nanotube aggregates. Patent Document 2 states that the median diameter of the CNT aggregate is 100 μm or less, but in Patent Document 2, it is stated that in the production of carbon nanotubes, milling treatment, i.e., polishing dispersion, is performed in ethanol to prepare the dispersion. However, there was a concern that polishing dispersion would affect the network structure of the CNT aggregate and lead to a decrease in conductivity. In contrast, the CNT aggregate according to the present disclosure satisfies conditions (1) and (2), resulting in excellent conductivity when used as a carbon nanotube dispersion, and the resulting carbon nanotube dispersion has an appropriate viscosity.

[0015] <Condition (1)> The CNT aggregate relating to this disclosure contains Na atoms, and the Na atom content is less than 200 ppm by mass relative to the total mass of the CNT aggregate.

[0016] The inclusion of sodium atoms in the CNT aggregate improves its hydrophilicity and thus its dispersibility in water-containing polar solvents. Specifically, the adsorption of sodium atoms onto the CNT surface changes the surface energy of the CNT, strengthening its interaction with the polar solvent. As a result, the CNT aggregate exhibits good dispersibility, making it easier to obtain a uniform dispersion. Furthermore, a sodium content of less than 200 ppm by mass is preferable because it does not lead to a decrease in battery performance when used as a conductive additive in lithium-ion batteries. Excessive sodium can cause side reactions within the battery and degrade battery performance, so it is important to maintain a sodium content within an appropriate range.

[0017] Furthermore, reducing the Na content to 10 ppm by mass is difficult from the standpoint of CNT synthesis and handling. Specifically, in the CNT manufacturing process, it is unavoidable that trace amounts of Na atoms are introduced as impurities from catalyst raw materials and reactors, making it technically difficult to achieve a Na content of less than 10 ppm by mass. Results from examples and comparative examples have confirmed that stable CNTs can be obtained in the manufacturing process if the Na content is 10 ppm by mass or more. Therefore, the Na atom content is preferably within the range described above. Within these ranges, the balance between conductivity and dispersibility of the CNT aggregate is optimized.

[0018] The lower limit of the Na atom content is not particularly limited and may be 0 ppm by mass. However, from a synthetic standpoint, it is technically difficult to reduce the Na atom content in the CNT aggregate to less than 10 ppm by mass. Specifically, in the CNT manufacturing process, it is unavoidable that trace amounts of Na atoms are mixed in as impurities from the catalyst raw materials and reactor. Therefore, it is difficult to achieve a Na atom content of less than 10 ppm by mass. The inventors' studies have confirmed that if the Na atom content is 10 ppm by mass or more, stable CNTs can be obtained in the manufacturing process. Furthermore, the inventors have confirmed that even if the Na atom content is 10 ppm by mass or more, there is almost no concern about a decrease in the conductivity or dispersibility of the CNT aggregate. The results of the examples and comparative examples described later also confirm that if the Na content is 10 ppm or more, stable CNTs can be obtained in the manufacturing process.

[0019] From the above viewpoint, the content of Na atoms relative to the total mass of the CNT aggregate according to this disclosure is less than 200 ppm by mass. Preferably, the content of Na atoms is 100 ppm by mass or less. Furthermore, the content of Na atoms may be 10 ppm by mass or more, preferably 12 ppm by mass or more, more preferably 15 ppm by mass or more, and even more preferably 20 ppm by mass or more. The content of Na atoms can be set by combining the above upper and lower limits. In one embodiment, the content of Na atoms is preferably 10 ppm by mass or more and less than 200 ppm by mass, more preferably 15 ppm by mass or more and 200 ppm by mass or less, and even more preferably 20 ppm by mass or more and 200 ppm by mass or less. In another embodiment, the content of Na atoms is preferably 10 ppm by mass or more and 100 ppm by mass or less, more preferably 15 ppm by mass or more and 100 ppm by mass or less, and even more preferably 20 ppm by mass or more and 100 ppm by mass or less. Within the above range, the dispersibility of the CNT aggregate when used as a dispersion, and the balance between the appropriate viscosity and conductivity of the dispersion can be optimized.

[0020] Methods to reduce the Na atom content to less than 200 ppm by mass include, for example, washing the CNT aggregate with water, acid, an acidic aqueous solution (for example, a 35% by mass aqueous solution of hydrochloric acid), or a chelating agent aqueous solution to reduce the Na atom content. Furthermore, the Na atom content can be adjusted by using methods such as immersing the CNT aggregate in an approximately 5% by mass aqueous solution of sodium nitrate or an approximately 5% by mass aqueous solution of sodium chloride to adsorb Na atoms onto the surface of the CNT aggregate, thereby increasing the Na atom content relative to the total mass of the CNT aggregate.

[0021] In this disclosure, the content of Na atoms relative to the total mass of a CNT aggregate (mass ppm) can be measured, for example, by the following method: The CNT aggregate is completely dissolved in an acid such as hydrochloric acid or nitric acid. Pretreatment such as dry ashing, wet ashing, or melting may be performed to completely dissolve the CNT aggregate in the acid. The content of Na atoms relative to the total mass of the CNT aggregate can be measured by performing inductively coupled plasma atomic emission spectroscopy (ICP-AES), inductively coupled plasma mass spectrometry (ICP-MS), etc., using the solution in which the CNT aggregate has been completely dissolved in the acid as a sample. From the viewpoint of achieving higher sensitivity measurements, it is preferable to perform ICP-MS.

[0022] Furthermore, when the Na atom content in a CNT aggregate is less than 10 ppm by mass, it becomes technically difficult to detect peaks originating from Na atoms, even when using ICP-MS, ICP-AES, etc., making it difficult to accurately calculate the content. For this reason, in this disclosure, if the Na atom content measured above is less than 10 ppm by mass, the Na atom content may be treated as 0, but this does not negate the presence of Na atoms in the CNT aggregate.

[0023] <Condition (2)> The CNT aggregate relating to this disclosure has a fracture elongation rate of more than 0% and 3.0% or less, as measured by the measurement method described below. (Method for measuring fracture elongation rate) A dispersion with a concentration of 0.20% by mass is prepared by mixing the carbon nanotube aggregate with water. The obtained dispersion is poured onto a 22 mm × 75 mm × 3 mm slide glass type silicon plate, and heated at 100°C for 30 minutes to dry and obtain a measurement sample. The obtained measurement sample is fixed to the gripping part of a tensile testing device, and a tensile test is performed at a speed of 1 mm / min. The point where the stress is maximum is considered the fracture point, and the fracture elongation rate is calculated from the length of the measurement sample at the fracture point and the length of the measurement sample before measurement.

[0024] The elongation at break of a CNT aggregate is measured, for example, by the following method: A carbon nanotube dispersion is prepared by mixing carbon nanotube aggregates, 700 kDa of carboxymethylcellulose sodium, and water, so that the concentration of carbon nanotube aggregates is 0.20 mass% and the concentration of carboxymethylcellulose sodium is 0.30 mass%. 15 mL of the prepared carbon nanotube dispersion is cast onto a 22 mm × 75 mm × 3 mm glass slide silicon plate (manufactured by Dosaka E-M Co., Ltd., #08-1044), and the dried film (CNT-containing film) is heated at 100°C for 30 minutes to prepare a measurement sample. The prepared measurement sample is fixed to the gripping part of a tensile testing device (manufactured by Shimadzu Corporation, Autograph AG-IS), and a tensile test is performed at a speed of 1 mm / min to calculate the tensile strength (MPa). At the same time, the point where the test force is maximum is considered the breaking point, and the elongation at break (%) is calculated. The elongation at break of the CNT aggregates relating to this disclosure is usually greater than 0% and 10.0% or less, and may be between 0.5% and 7.0%, between 0.7% and 5.0%, between 1.0% and 4.5%, between 1.3% and 4.0%, or between 1.5% and 3.5%. In particular, the elongation at break of the CNT aggregates is preferably between 1.5% and 3.0%.

[0025] If the elongation at break of the CNT aggregate according to this disclosure is 1.5% or more, the length of the CNTs is sufficiently long, making it easier to ensure conductivity. Specifically, the sufficient length of the CNTs increases the number of contact points between the CNTs, allowing for smoother electron movement, thus improving the conductivity of the entire CNT aggregate. Furthermore, by maintaining an appropriate length of the CNTs, conductive paths are efficiently formed, optimizing conductivity. If the elongation at break of the CNT aggregate according to this disclosure is 3.0% or less, it is easy to process into a dispersion, and dispersibility in the dispersion is easily ensured. Specifically, an elongation at break of 3.0% or less maintains an appropriate degree of flexibility of the CNTs, enabling uniform dispersion of the CNTs in the dispersion. This appropriately maintains the viscosity of the dispersion, improving dispersibility. Therefore, by having the elongation at break within the above range, the conductivity and dispersibility of the CNT aggregate are improved.

[0026] <Condition (3)> The CNT aggregate according to the present disclosure preferably has a cumulative 50% particle size D50 in the volume-based particle size distribution that is 1.0 μm or more and 15 μm or less. The CNT aggregate according to the present disclosure preferably has a cumulative 50% particle size D50 in the volume-based particle size distribution that is 1.0 μm or more and 14 μm or less, and even more preferably 1.0 μm or more and 13.5 μm or less. By having the cumulative 50% particle size D50 within the above range, the particle size of the CNT aggregate is appropriately controlled, and uniform dispersion of the CNT aggregate in the dispersion is achieved. In particular, when the cumulative 50% particle size D50 is in the range of 1.0 μm or more and 15 μm or less, the particle size of the CNT aggregate is appropriately small and uniform, so aggregation of the CNT aggregate in the dispersion is suppressed and dispersibility is improved. The small particle size of the CNT aggregate increases its surface area in the dispersion, strengthening its interaction with the dispersion medium and thus improving dispersibility. Furthermore, a uniform particle size distribution stabilizes the viscosity of the CNT aggregate dispersion, resulting in better processability and handling when forming electrodes or other components using the CNT aggregate. Moreover, when the cumulative 50% particle size D50 is within the above range, the particle size of the CNT aggregate is appropriately controlled, achieving more uniform dispersion when preparing dispersions using the CNT aggregate. Therefore, by satisfying condition (3), the dispersibility of the CNT aggregate is further improved and the viscosity of the dispersion is optimized, making it possible to provide a high-performance CNT dispersion with excellent conductivity and handling properties.

[0027] The cumulative 50% particle size D50 in the volume-based particle size distribution of a CNT aggregate is measured as follows: The CNT dispersion is thoroughly stirred and then diluted with pure water. The resulting diluted solution is used as a sample, and the cumulative particle size D50 of the CNT dispersion is measured using a particle size analyzer (LA-960, laser diffraction particle size analyzer, Horiba, Ltd.). The particle refractive index of the CNTs to be measured is assumed to be 1.920–0.522i. The refractive index of the solvent is assumed to be 1.333. During measurement, the CNT dispersion is diluted by dropping it into pure water while observing the transmittance, and the measurement is performed after confirming that the particle size distribution on the monitor is stable.

[0028] <Other matters concerning CNT aggregates> In this disclosure, the CNTs included in the CNT aggregate may be SWCNTs or MWCNTs. From the viewpoint that having a layer distribution and slightly lower uniformity contributes to satisfying conditions (1) and (2), it is preferable that the CNT aggregate includes SWCNTs and MWCNTs.

[0029] The maximum length of the CNTs included in the CNT aggregate relating to this disclosure is not particularly limited.

[0030] In one embodiment, the CNT aggregate may mainly consist of CNTs with a maximum length of 500 μm or less, and may not contain CNTs with a length greater than 500 μm and less than or equal to 30,000 μm. Here, "main component" means that 90% by mass or more of the CNTs constituting the CNT aggregate are CNTs with a maximum length of 500 μm or less. The CNT aggregate may also contain CNTs with a maximum length of 500 μm or less.

[0031] The CNT aggregates according to this disclosure include, for example, CNTs having a maximum length of 10 μm to 30,000 μm. The CNT aggregates according to this disclosure preferably include CNTs having a maximum length of 500 μm or more, more preferably include CNTs having a maximum length of 500 μm to 30,000 μm, and even more preferably include CNTs having a maximum length of 1,000 μm to 30,000 μm (i.e., ULCNTs).

[0032] ULCNTs are longer in length and can take the form of fibers compared to general-purpose CNTs. When the maximum length of the CNTs included in the CNT aggregate according to this disclosure is 500 μm or more, the entanglement between the CNTs becomes moderately strong, and the CNTs tend to form a network structure more easily.

[0033] By taking the form of fibers, ULCNTs have a tendency to entangle with each other. A CNT aggregate is preferably an aggregate containing multiple ULCNTs, as this allows the CNTs to entangle with each other and form a more stable aggregate. Hereinafter, an aggregate containing ULCNTs may be abbreviated as an "ULCNT aggregate."

[0034] Here, the term "fiber" is generally used to refer to a structure in which one dimension is larger than the other two dimensions. The fiber may be a thread-like fiber with a circular cross-section, a ribbon-like fiber with a rectangular cross-section, hollow, or have other shapes. From the viewpoint of improving conductivity, the cross-section of the CNTs contained in the CNT aggregate is preferably circular and preferably hollow.

[0035] The CNT aggregate may be an aggregate of three-dimensional structures in which the CNTs are intertwined. The intertwined state of the CNTs in the CNT aggregate according to this disclosure can be confirmed by SEM observation.

[0036] The length of individual carbon nanotubes (CNTs) within a CNT aggregate can be measured by focusing on a single CNT and observing multiple SEM images within adjacent fields of view. Here, "CNT length" refers to the measured length in the longitudinal direction of the CNT, and the maximum value among the measured lengths is defined as the "maximum length." If, by observing the SEM images, one CNT with a maximum length in the range of 1,000 μm to 30,000 μm is observed within the field of view of the SEM image, it can be confirmed that the observed CNT contains a ulcerative colloidal cell (ULCNT).

[0037] It is preferable that multiple ULCNs are present within the field of view of the SEM image. Focusing on 100 CNTs included in the field of view of the SEM image, the maximum length of each is measured, and of the observed CNTs, it is preferable that 10% or more (in numerical terms) of the CNTs have a maximum length in the range of 1000 μm to 30000 μm (i.e., ULCNs), from the viewpoint of further improving the stability of the CNT aggregate due to the entanglement of ULCNs, more preferably 20% or more, even more preferably 30% or more, and particularly preferably 50% or more.

[0038] The diameter of an ULCNT can be measured by observing a SEM (Surface-Emission Microscope) or transmission electron microscope (TEM) image. Here, diameter refers to the length in the direction perpendicular to the longitudinal direction of the ULCNT. The diameter of an ULCNT is determined by measuring the diameter at 10 different points on a single ULCNT and taking the average value of these measurements.

[0039] The length of the ULCNT is in the range of 1,000 μm to 30,000 μm, preferably in the range of 1,050 μm to 25,000 μm, more preferably in the range of 1,100 μm to 20,000 μm, even more preferably in the range of 1,200 μm to 18,000 μm, and particularly preferably in the range of 1,300 μm to 15,000 μm. The diameter of the ULCNT is preferably in the range of 1 nm to 100 nm, more preferably in the range of 2 nm to 80 nm, even more preferably in the range of 3 nm to 50 nm, and particularly preferably in the range of 5 nm to 30 nm.

[0040] The length / diameter ratio, or aspect ratio, of the ULCNT is preferably 1000 or more, more preferably 3000 or more, even more preferably 5000 or more, and particularly preferably 10000 or more. The aspect ratio can be calculated from the ratio of the maximum length to the diameter of a single ULCNT. From the viewpoint of measurement accuracy, it is preferable to use the average value of the measurements of 20 or more ULCNTs.

[0041] Furthermore, from the viewpoint of dispersibility, the specific gravity of the ULCNT aggregate is preferably in the range of 1.5 to 2.5, more preferably in the range of 1.7 to 2.4, and even more preferably in the range of 1.8 to 2.2. The specific gravity of the ULCNT aggregate can be measured by the method described in JIS Z8807:2012 "Method for measuring the density and specific gravity of solids".

[0042] The purity of carbon as CNTs in an ULCNT aggregate can be measured by thermomass spectrometry. For example, a thermomass (TG) curve and differential thermal analysis (DTA) curve of the ULCNT aggregate are obtained using a thermal analyzer (Shimadzu Corporation, DTG-60). In the DTA curve, where the peak top appears around 650°C to 750°C, the largest exothermic peak is considered to be the combustion of CNTs, and other exothermic peaks are considered to be the combustion of substances other than CNTs. The purity of the CNTs is determined from the mass loss rate of the TG curve. From the viewpoint of the resulting conductivity, the purity of the ULCNT aggregate is preferably 50% by mass or more, more preferably 65% ​​by mass or more, even more preferably 80% by mass or more, and particularly preferably 95% by mass or more.

[0043] The resulting fibrous ULCNT is preferably flexible and strong. Furthermore, the conductivity of the ULCNT itself should be 5000 ohms. －１ ・m －１ Preferably, it is 10,000 ohms or more. －１ ・m －１ The above is more preferable. The conductivity of the ULCNT itself is typically 1,000,000 ohms. －１ ・m －１ The following applies:

[0044] <Method for producing CNTs> The method for producing CNTs in this disclosure is not particularly limited. For example, the method for producing CNTs in this disclosure can be a conventionally known chemical vapor deposition (CVD) method, a method of reacting a gaseous reactant containing a carbon source in the presence of a catalyst, or other such methods.

[0045] The CNTs in this disclosure can be manufactured by referring to, for example, the methods described in Japanese Patent Publication No. 2016-102047, Japanese Patent Publication No. 2021-527611, etc.

[0046] The following describes the manufacturing method of CNTs in this disclosure with examples. However, the manufacturing method of CNTs in this disclosure is not limited to the following examples.

[0047] =Manufacturing Method X= An example of a method for manufacturing CNTs as referenced in this disclosure is the manufacturing method described in Japanese Patent Application Publication No. 2016-102047. That is, a manufacturing method (hereinafter also referred to as "Manufacturing Method X") that includes the steps of passing a gaseous reactant containing one or more carbon sources through a reactor, reacting one or more gaseous reactants in the reaction region of the reactor in the presence of a catalyst to form carbon-containing product particles, agglomerating the product particles into aggregates, and applying force to the aggregates to continuously move the aggregates out of the reaction region.

[0048] According to manufacturing method X, CNTs containing ULCNTs can be obtained in the form of easily handled fibrous aggregates or other aggregates.

[0049] In manufacturing method X, the force applied to the product particles may be a mechanical force. If the aggregate is fibrous CNT, the mechanical force applied to the product particles can be applied by a rotating spindle around which the aggregate is wound. The fibrous CNT may be collected on the spindle, or it may be accumulated elsewhere after being rotated around the spindle once or more times, as the spindle is continuously unwound.

[0050] Preferably, the spindle axis is positioned perpendicular or parallel to the flow direction of one or more gaseous reactants, but it may be positioned in other orientations. For example, a spindle with its axis positioned at a 25° angle to the flow direction of the gaseous reactants can also be suitably used to apply mechanical force to product particles.

[0051] The spindle can rotate around two axes (for example, two vertical axes). In particular, the spindle can rotate around axes perpendicular and parallel to the flow direction of the gaseous reactant. Such a spindle allows for the pulling and twisting of aggregates, which are fibrous carbon nanotubes, to control the number of twists and length.

[0052] The spindle material may be metal, ceramic, or resin. The spindle can take on different suitable shapes depending on the material properties and the intended use of the CNTs. The spindle can be used, for example, as a mold for producing carbon products by a spin-coating process. Preferred spindle shapes are rod-shaped or box-shaped.

[0053] Fibrous carbon nanotubes (CNTs) are accumulated on the spindle or elsewhere, and the coating thickness and orientation can be controlled by controlling the reaction time and reaction conditions, or by applying an electric field or other field to the carbon product. The coating thickness and orientation of the carbon product can be controlled, for example, by the fluidity of the gas.

[0054] The spindle rotation speed is preferably 0.01 rpm (revolutions per minute; the same applies hereafter) to 10,000 rpm, and more preferably 0.1 rpm to 100 rpm. The spinning speed (i.e., the spindle rotation speed) may be adjusted so that the material is recovered at the same rate as it is produced. The spindle rotation speed may be used to control the thickness of the accumulated fibrous CNTs. In one preferred embodiment, as the spindle rotates, the fibrous CNTs are processed in the axial direction of the spindle. In this processing, the fibrous CNTs are wound evenly along the spindle, rather than being wound at only one specific point on the spindle.

[0055] Fibrous CNTs may be recovered onto the reactor wall, for example, by a substrate placed in the reactor. The substrate may be a fixed substrate or a rotating guide used to apply a strong and equal force to the fibrous CNTs when they are recovered. A suitable substrate arrangement used in fiber technology is a substrate consisting of two guides positioned orthogonally to each other.

[0056] In manufacturing method X, the mechanical force applied to the product particles may be a force applied by an accelerating gas flow. The accelerating gas flow can be generated by passing the product particles through a reactor having a narrow diameter or through a capillary tube located downstream of the reaction region. A vacuum may be applied to the product particles.

[0057] Other forces applied to the product particles include electrostatic forces appropriately applied by a charged plate. When using electrostatic forces, the product particles must be charged. By using a charged plate, CNTs can be generated on the plate in the form of intertwined sheets.

[0058] Furthermore, other forces applied to the generated particles may include magnetic force or photon pressure applied by a light source.

[0059] The raw material for CNTs may be injected in the form of a liquid containing a carbon source, instead of a gaseous reactant containing a carbon source. When a liquid is used as the raw material for CNTs, it can be injected through a single inlet or multiple inlets, for example, in a showerhead configuration.

[0060] One or more gaseous reactants are preferably reacted at 500°C to 1600°C, and more preferably at 1000°C to 1500°C. The temperature gradient is maintained within the reactor, and the reaction region is preferably kept at a higher temperature than the product region of the reactor.

[0061] The gaseous reactant may be used in combination with one or more gases that act as diluents. The gaseous reactant may also be used in combination with gases that do not play a direct role in the reaction but play an auxiliary role. If amorphous carbon is produced as a byproduct, it is also preferable to use a gas as a diluent that can react with amorphous carbon to maintain the reaction sites on the catalyst and produce nanotubes.

[0062] Gases that can be used as diluents include argon or other inert gases, hydrogen, nitrogen, ammonia, carbon dioxide, and helium. Among these, hydrogen is particularly preferred as a diluent.

[0063] The composition of the product particles can be controlled by monitoring the aggregates and changing the reaction conditions based on the information obtained. For example, aggregates can be monitored by online Raman spectroscopy. Online Raman spectroscopy provides data indicating whether the CNTs are single-layer or multi-layer. It also provides data indicating the diameter and crystallinity of the CNTs. Aggregates can also be monitored by online conductivity measurement, gas analysis, measurement of the opacity of the reaction region, and / or measurement of the winding force.

[0064] When removing aggregates from the reactor, it is preferable to prevent air from entering the reactor. Preventing air inflow is particularly important, for example, when the diluent gas contains hydrogen, as it helps to prevent the formation of an explosive mixture of hydrogen and air in the reactor.

[0065] The product particles produced in manufacturing method X contain ULCN. Depending on the manufacturing conditions, SWCNTs and MWCNTs may also be present.

[0066] The product particles may be generated by chemical vapor deposition. When the product particles are generated by chemical vapor deposition, the carbon source, which is a gaseous reactant, reacts in the presence of a catalyst.

[0067] Suitable carbon-containing compounds as carbon sources include carbon monoxide, carbon dioxide, aromatic hydrocarbons (e.g., benzene, toluene, xylene, cumene, ethylbenzene, naphthalene, or mesitylene), non-aromatic hydrocarbons (e.g., methane, ethane, propane, butane, pentane, hexane, cyclohexane, ethylene, propylene, or acetylene), and oxygen-containing hydrocarbons (e.g., formaldehyde, acetaldehyde, acetone, methanol, ethanol, diethyl ether, polyethylene glycol, 1-propanol, ethyl formate, or hydrocarbons containing two or more of these). Carbon monoxide, methane, ethylene, or acetylene are preferred as carbon-containing compounds.

[0068] The carbon source preferably contains oxygen. Ethanol is a particularly preferred carbon source. Oxygen can be introduced into the reactor by other means, for example, by using a carbon source containing a diluent gas or water.

[0069] As catalysts, transition metals are preferred, particularly chromium (Cr), molybdenum (Mo), tungsten (W), or VIII-B transition metals. Specifically, preferred catalysts include, for example, iron (Fe), cobalt (Co), nickel (Ni), ruthenium (Ru), rhodium (Rh), palladium (Pd), osmium (Os), iridium (Ir), and platinum (Pt) or manganese (Mn), or mixtures thereof. Metals from the lanthanide and actinide series (e.g., yttrium (Y)) can also be used as catalysts. Fe, Ni, Co, Mo, and mixtures thereof are preferred, for example, a mixture of Ni and Co (mass ratio: 50 / 50), a mixture of Fe and Ni, or a mixture of Fe and Mo are more preferred. Any of these transition metals can be used alone or in combination with any of the other transition metals listed above to function as catalysts for the growth of CNTs. The catalyst is particularly preferably a mixture of two or more of the listed metals.

[0070] The catalyst is preferably formed by the decomposition of a precursor. The precursor is preferably a thermal, photocatalytic, or plasma-degradable compound of one or more of the above-mentioned metals, such as a carbonyl or cyclopentadienyl organometallic compound. Ferrocene, iron pentacarbonyl, nickelocene, and cobaltocene are particularly preferred as precursors. In one embodiment, at least 0.01% by mass of the precursor is contained in the carbon source, preferably 0.2% to 30% by mass of the precursor, and more preferably 0.2% to 20% by mass of the precursor. In another embodiment, 0.23% to 2.3% by mass of the precursor may be contained in the carbon source, and 0.02% to 20% by mass of the precursor. The catalyst may also be used supported on a carrier. Preferred carriers include silica and magnesium oxide.

[0071] The carbon source is preferably reacted in the presence of an accelerator. Suitable accelerators are one or more of sulfur, phosphorus, molybdenum, and organic compounds of these elements. Thiophene is also a preferred accelerator. Preferably, the accelerator is contained in the carbon source at a concentration of up to 10% by mass. Preferably, the accelerator is contained in the carbon source at a concentration of 0.2% to 6% by mass. When high or low concentrations of thiophene are used as the accelerator, MWCNTs are formed.

[0072] According to manufacturing method X, fibrous CNTs having a length of at least 500 μm, for example, at least 1 mm, can be obtained. The fibrous CNTs can take the form of threads or sheets. The length of the fibrous CNTs can be controlled, for example, by the winding capacity of the spindle used when manufacturing the fibrous CNTs.

[0073] The manufacturing method X preferably includes the steps of generating CNTs by reacting a carbon source in the reaction region of a reactor, and agglomerating the CNTs into aggregates by applying force to them. This manufacturing method makes it possible to easily produce fibrous CNTs.

[0074] The manufacturing method X preferably further includes a step of passing the obtained CNT aggregates through a sieve after the step of agglomerating the CNTs into aggregates. It is also preferable to recover the CNTs that have passed through the sieve. By passing the obtained CNT aggregates through a sieve, CNT aggregates that satisfy conditions (1) and (2) are more easily obtained.

[0075] The method of passing the material through the sieve is not particularly limited and can be carried out by commonly known methods. The mesh size of the sieve is, for example, 0.1 mm to 3.0 mm, preferably 0.5 mm to 2.0 mm, and more preferably 1.0 mm to 1.5 mm. The material of the sieve is not particularly limited and may be metal or resin. When the CNT aggregate is applied to an electrode (especially an electrode of a lithium-ion battery), it is preferable that the material does not impair the performance of the battery. The number of times the material is passed through the sieve is, for example, 1 to 3 times. Before passing the CNT aggregate through the sieve, the CNT aggregate may be cut into appropriate sizes beforehand.

[0076] Also, it is preferable to pass the material through a sieve two or more times using two types of sieves with different mesh sizes. By using the sieve with a relatively smaller mesh size among the two types of sieves, it is possible to remove amorphous carbon or the like that has become powdery. Also, by using the sieve with a relatively larger mesh size among the two types of sieves, it is possible to remove foreign substances mixed in from the outside, coarse CNTs, etc.

[0077] By passing the obtained CNT aggregates through a sieve and collecting the CNTs that have passed through the sieve, coarse CNTs are removed and the stability of the CNT dispersion is improved. Also, generally in the production of electrodes, foreign substances mixed in from the outside are removed, but by passing the obtained CNT aggregates through a sieve, it is possible to more easily remove foreign substances mixed in from the outside.

[0078] As another aspect, after generating CNTs containing ULCNT by the above method in the reaction region, condensing to form CNTs containing ULCNT, and continuously withdrawing CNTs from near the reaction region, a means including these steps may be employed. Also, as another aspect, a means including generating CNTs containing ULCNT in the reaction region, continuously electrostatically attracting CNTs containing ULCNT from the reaction region, and collecting CNTs containing ULCNT may be employed.

[0079] = Production Method Y = In the present disclosure, as an example of a method for producing CNTs, the production method described in Japanese Patent Application Laid-Open No. 2021-527611 can be referred to. That is, a production method (hereinafter, also referred to as "Production Method Y") including a step (1) of producing an active support by supporting a mixture containing a main catalyst precursor and a cocatalyst precursor on γ-Al ２ O ３ ; a step (2) of drying the active support by multi-stage drying including vacuum drying; a step (3) of producing a supported catalyst by subjecting the dried active support to heat treatment; and a step (4) of producing CNTs in the presence of the supported catalyst.

[0080] - Step (1) In step (1), an active support is produced by supporting a mixture containing a main catalyst precursor and a cocatalyst precursor on γ-Al ２ O ３ . <

[0081] The main catalyst precursor and co-catalyst precursor are γ-Al ２ O ３ To ensure uniform support, the mixture may further contain a solvent, and the main catalyst precursor and co-catalyst precursor may be dissolved in the solvent. The solvent may be one or more selected from the group consisting of water, methanol, and ethanol, with water being preferred.

[0082] γ-Al ２ O ３ Because it has high porosity and a spinel structure, the main catalyst and co-catalyst are γ-Al ２ O ３ They can be arranged irregularly. CNTs grown from an irregularly arranged main catalyst can be produced in an entangled manner.

[0083] The main catalyst may be one or more selected from the group consisting of cobalt, iron, nickel, manganese, and chromium, with cobalt being preferred.

[0084] The main catalyst precursor may be one or more selected from the group consisting of nitrates, sulfates, carbonates, and acetates of the main catalyst, with nitrates of the main catalyst being preferred.

[0085] The main catalyst precursor is Co(NO ３ ) ２ Co(NO ３ ) ２ 6H ２ O, Co ２ (CO) ８ Co ２ (CO) ６ [HC=C(C(CH ３ ) ３ ) ], Co (CH ３ CO ２ ) ２ Fe(NO ３ ) ３ Fe(NO ３ ) ２ nH ２ O, Fe(CH ３ CO ２ ) ２ Ni (NO ３ ) ２ Ni (NO ３ ) ２ 6H２ O, Mn (NO ３ ) ２ , Mn(NO ３ ) ２ 6H ２ O, Mn(CH ３ CO ２ ) ２ ・n(H ２ O) and Mn(CO) ５ It may be one or more selected from the group consisting of Br, and among these, Co(NO ３ ) ２ 6H ２ O, Fe (NO ３ ) ２ nH ２ O, Ni (NO ３ ) ２ 6H ２ O is preferred.

[0086] The co-catalyst improves the dispersibility of the main catalyst and may be one or more selected from the group consisting of vanadium and molybdenum.

[0087] The co-catalyst precursor is NH ４ VO ３ NaVO ３ , V ２ O ５ , V(C ５ H ７ O ２ ) ３ , and (NH ４ ) ６ Mo ７ O ２４ 4H ２ It may be one or more selected from the group consisting of O, and NH ４ VO ３ and (NH ４ ) ６ Mo ７ O ２４ 4H ２ It is preferable to select one or more from the group consisting of O.

[0088] When the mixture contains two or more co-catalyst precursors, that is, when it contains both a vanadium precursor and a molybdenum precursor, the molar ratio of the sum of vanadium and molybdenum to vanadium can be 1:0.45 to 1:0.95 or 1:0.5 to 1:0.9, and is preferably 1:0.5 to 1:0.9. When the above conditions are met, the structure of the CNTs can be stably maintained and CNTs with the desired pore volume can be produced.

[0089] The mixture may contain a main catalyst precursor and a co-catalyst precursor in molar ratios of 1:0.01 to 1:0.5, 1:0.1 to 1:0.4, or 1:0.1 to 1:0.25, with a preferred ratio of 1:0.1 to 1:0.25. Satisfying the above molar ratios improves the dispersibility of the main catalyst, enabling the production of CNTs with the desired pore volume.

[0090] The mixture may further contain an organic acid that plays a role in suppressing the precipitation of the main catalyst precursor and the co-catalyst precursor.

[0091] The organic acid may be one or more selected from the group consisting of citric acid, tartaric acid, fumaric acid, malic acid, acetic acid, butyric acid, palmitic acid, and oxalic acid, with citric acid being preferred.

[0092] The mixture can contain the organic acid and the co-catalyst precursor in a molar ratio of 1:1 to 1:20, 1:2 to 1:10, or 1:3 to 1:6, with a ratio of 1:3 to 1:6 being preferred. Satisfying the above range has the advantage of enabling the production of a transparent catalyst metal solution during catalyst manufacturing and the production of a catalyst with suppressed fine powder formation during impregnation.

[0093] The process may further include a maturation step after step (1).

[0094] The maturation process may be carried out for 1 to 60 minutes or 10 to 50 minutes. It is preferable to carry it out for 10 to 50 minutes. When the above conditions are met, γ-Al ２ O ３The main catalyst precursor and co-catalyst precursor can be sufficiently supported on the support. Furthermore, bubbles present within the support are removed to the maximum extent possible, allowing the main catalyst precursor and co-catalyst precursor to be sufficiently supported even in the fine pores inside the support.

[0095] Step (2) Next, the active support is dried by multi-stage drying, which includes vacuum drying.

[0096] Multi-stage drying can mean that a drying process, including vacuum drying, is performed two or more times. Specifically, multi-stage drying may include atmospheric pressure drying and vacuum drying, or it may include vacuum drying alone two or more times.

[0097] Vacuum drying may be carried out at 80°C to 300°C or 120°C to 250°C, with 120°C to 250°C being preferred. When the above conditions are met, the main catalyst precursor, i.e., the coordination bond of the main catalyst, can be easily decomposed to form the main catalyst oxide, and energy consumption can be minimized.

[0098] Vacuum drying may be performed at 1 mbar to 200 mbar or 30 mbar to 150 mbar, and is preferably performed at 30 mbar to 150 mbar. When the above conditions are met, the main catalyst precursor, i.e., the coordination bond of the main catalyst, is rapidly decomposed and discharged, so that the main catalyst oxide can be formed more easily under vacuum conditions and energy consumption can be minimized.

[0099] Vacuum drying can be performed for 10 minutes to 3 hours or 10 minutes to 2 hours, with 10 minutes to 2 hours being preferred. When the above conditions are met, the main catalyst precursor can be easily decomposed and converted into the main catalyst oxide, and energy consumption can be minimized.

[0100] On the other hand, if multi-stage drying includes atmospheric pressure drying and vacuum drying, atmospheric pressure drying can be performed before the vacuum drying described above, and atmospheric pressure drying can remove any solvents that may be present in the active carrier.

[0101] Atmospheric pressure drying may be carried out at 80°C to 160°C or 100°C to 140°C, and is preferably carried out at 100°C to 140°C. When the above conditions are met, the solvent present in the active carrier can be sufficiently removed, and energy consumption can be minimized.

[0102] Atmospheric pressure drying may be carried out at 900 mbar to 1,100 mbar, and preferably at 950 mbar to 1,050 mbar. When the above conditions are met, the solvent present in the active carrier can be sufficiently removed, and energy consumption can be minimized.

[0103] Atmospheric pressure drying may be carried out for 1 to 12 hours, and preferably for 3 to 9 hours. When the above conditions are met, the solvent present in the active carrier can be sufficiently removed, and energy consumption can be minimized.

[0104] On the other hand, if multi-stage drying includes two or more vacuum drying steps, it may include two or more vacuum drying steps performed at different temperatures, more specifically, a primary vacuum drying step performed at a first temperature and a secondary vacuum drying step performed at a second temperature higher than the first temperature.

[0105] Primary vacuum drying can remove any solvents that may be present in the active carrier.

[0106] The first temperature may be between 80°C and 160°C, and is preferably between 100°C and 140°C. When the above conditions are met, the solvent present in the active carrier can be sufficiently removed, and energy consumption can be minimized.

[0107] Primary vacuum drying can be performed for 1 to 12 hours, preferably 3 to 9 hours. When the above conditions are met, the solvent present in the active carrier can be sufficiently removed, and energy consumption can be minimized.

[0108] Primary vacuum drying may be performed at 1 mbar to 200 mbar, 1 mbar to 150 mbar, or 80 mbar to 150 mbar, with 80 mbar to 150 mbar being preferred. When the above conditions are met, the solvent present in the active carrier can be sufficiently removed, and energy consumption can be minimized.

[0109] The explanation regarding secondary vacuum drying is as described in the explanation of vacuum drying above.

[0110] The second temperature may be 175 to 300°C, and is preferably 180 to 280°C. When the above conditions are met, the main catalyst precursor, i.e., the coordination bond of the main catalyst, can be easily decomposed to form the main catalyst oxide, and energy consumption can be minimized.

[0111] Secondary vacuum drying may be performed at 1 mbar to 200 mbar, 1 mbar to 150 mbar, or 1 mbar to 70 mbar, with 1 mbar to 70 mbar being more preferable. When the above conditions are met, the main catalyst precursor, i.e., the coordination bond of the main catalyst, is rapidly decomposed and discharged, so that the main catalyst oxide can be formed more easily under vacuum conditions and energy consumption can be minimized.

[0112] Secondary vacuum drying may be performed for 10 minutes to 3 hours or 10 minutes to 2 hours, and is preferably performed for 10 minutes to 2 hours. When the above conditions are met, the main catalyst precursor can be easily decomposed and converted into the main catalyst oxide, and energy consumption can be minimized.

[0113] Step (3) Next, the dried active support is subjected to heat treatment to produce a supported catalyst.

[0114] When heat treatment is performed, the main catalyst and co-catalyst are converted into γ-Al ２ O ３ A supported catalyst is manufactured that exists as a coating on the surface and pores of the material.

[0115] The heat treatment may be carried out at 600°C to 800°C or 620°C to 750°C, and is preferably carried out at 620°C to 750°C. When the above conditions are met, the main catalyst and co-catalyst are γ-Al２ O ３ The supported catalyst can be produced in a state where it is uniformly coated on the surface and pores of O, and the energy consumption can be minimized.

[0116] The heat treatment may be carried out for 1 hour to 12 hours or 2 hours to 8 hours, and it is preferably carried out for 2 hours to 8 hours. When the above time is satisfied, the supported catalyst existing in a state where it is uniformly coated on the surface and pores of γ-Al ２ O ３ can be produced.

[0117] - Step (4) Next, CNTs are produced in the presence of the supported catalyst.

[0118] Specifically, CNTs can be produced by bringing the supported catalyst into contact with a carbon-based compound. Specifically, a chemical vapor synthesis method may be used.

[0119] Regarding the step of producing CNTs in detail, first, the supported catalyst can be introduced into a horizontal fixed-bed reactor or a fluidized-bed reactor. Next, a carbon-based compound in a gaseous state or a mixed gas of a carbon-based compound in a gaseous state, a reducing gas (e.g., hydrogen, etc.) and a carrier gas (e.g., nitrogen, etc.) at a temperature not lower than the thermal decomposition temperature of the carbon-based compound in a gaseous state or not higher than the melting point of the catalyst supported on the supported catalyst is injected, and CNTs can be grown by chemical vapor synthesis by the decomposition of the carbon-based compound in a gaseous state.

[0120] The CNTs produced by the chemical vapor synthesis method as described above may have a crystal growth direction substantially parallel to the tube axis, and may have high crystallinity of a graphite structure in the tube length direction. As a result, CNTs having a small unit diameter, high conductivity and high strength can be produced.

[0121] The chemical vapor synthesis method may be carried out at 600°C to 800°C or 650°C to 750°C, and it is preferably carried out at 650°C to 750°C. When the above temperature is satisfied, CNTs can be produced while minimizing the generation of amorphous carbon.

[0122] Possible heat sources for the reaction include induction heating, radiant heat, lasers, IR, microwaves, plasma, and surface plasmon heating.

[0123] Furthermore, carbon-based compounds can be used without particular restrictions, as long as they can supply carbon and exist in a gaseous state at temperatures above 300°C.

[0124] The carbon-based compound may be a carbon-based compound having six or fewer carbon atoms, and may be one or more selected from the group consisting of carbon monoxide, methane, ethane, ethylene, ethanol, acetylene, propane, propylene, butane, butadiene, pentane, pentene, cyclopentadiene, hexane, cyclohexane, benzene, and toluene.

[0125] After growing CNTs by the reaction described above, a cooling step may be selectively performed to further align the CNTs in a more regular manner. Specifically, the cooling step can be carried out by natural cooling by removing the heat source or by using a cooler or the like.

[0126] The above-described manufacturing methods X and Y are examples, and the manufacturing methods for CNTs that may be included in a CNT aggregate are not limited to those described above.

[0127] [Carbon Nanotube Dispersion] A carbon nanotube dispersion (CNT dispersion) can be prepared using the CNT aggregate according to this disclosure. The CNT dispersion comprises the CNT aggregate and a dispersion medium. The CNT dispersion exhibits good dispersibility of the CNT aggregate according to this disclosure in the dispersion medium and has excellent conductivity. The CNT dispersion is preferably used for electrode formation, transparent conductive film formation, resin additives, conductive inks, coatings, antistatic agents, paints, etc.

[0128] <CNT aggregates> The CNT aggregates contained in the CNT dispersion are the same as the CNT aggregates related to this disclosure described above, so their explanation is omitted here.

[0129] <Dispersion Medium> The dispersion medium preferably contains water, and more preferably contains water as its main component. "Containing water as its main component" means that the proportion of water in the dispersion medium is more than 50% by mass. The proportion of water in the dispersion medium is preferably 90% by mass or more, more preferably 95% by mass or more, even more preferably 99% by mass or more, and may be, for example, 100% by mass.

[0130] The water is not particularly limited, but it is preferable to use distilled water, deionized water, or pure water, for example, because it contains fewer impurities.

[0131] The dispersion medium may be a mixture of water and a hydrophilic solvent. Examples of hydrophilic solvents include carbonate compounds such as ethylene carbonate, propylene carbonate, dimethyl carbonate, diethyl carbonate, methyl ethyl carbonate, and butylene carbonate; ether compounds such as tetrahydrofuran; ketone compounds such as acetone; lower alcohol compounds such as methanol and ethanol; and solvents such as acetonitrile. When the dispersion medium contains a hydrophilic solvent, the proportion of the hydrophilic solvent in the dispersion medium is preferably 10% by mass or less, more preferably 5% by mass or less, and even more preferably 1% by mass or less.

[0132] The CNT dispersion may further contain other components that can be used in the dispersion, in addition to the CNT aggregate and dispersion medium. Examples of other components include dispersants, defoamers, antistatic agents, and conductive additives other than the conductive additives described herein. It may also further contain trace amounts of impurities, so-called unavoidable impurities.

[0133] <Dispersant> The CNT dispersion may contain a dispersant for the purpose of further improving the dispersibility and dispersion stability of the CNT aggregate. The dispersant is not particularly limited and, for example, various surfactants can be used. Polymer compounds such as resins can also be used as dispersants. A surfactant is preferred as the dispersant. The surfactant may be an ionic surfactant or a nonionic surfactant and is not particularly limited. In the CNT dispersion, the surfactant can be used alone or in a mixture of two or more types.

[0134] Examples of ionic surfactants include anionic surfactants, cationic surfactants, and amphoteric surfactants. Examples of anionic surfactants include aromatic sulfonic acid-based surfactants such as alkylbenzene sulfonates (e.g., dodecylbenzenesulfonic acid) and dodecylphenyl ether sulfonates; ether sulfate-based surfactants; phosphate-based surfactants; and carboxylic acid-based surfactants. Examples of cationic surfactants include alkylamine salts and quaternary ammonium salts. Examples of amphoteric surfactants include alkylbetaine-based surfactants and amine oxide-based surfactants. As for ionic surfactants, ionic surfactants having an aromatic ring (so-called aromatic ionic surfactants) are preferred, and aromatic sulfonic acid-based surfactants such as alkylbenzene sulfonates and dodecylphenyl ether sulfonates are more preferred. Aromatic ionic surfactants tend to have excellent dispersibility, dispersion stability, and high concentration properties for CNT aggregates.

[0135] Examples of nonionic surfactants include sugar ester surfactants such as sorbitan fatty acid esters and polyoxyethylene sorbitan fatty acid esters; fatty acid ester surfactants such as polyoxyethylene resin acid esters and polyoxyethylene fatty acid diethyl; ether surfactants such as polyoxyethylene alkyl ethers, polyoxyethylene alkylphenyl ethers, and polyoxyethylene polypropylene glycol; and aromatic nonionic surfactants such as polyoxyalkylene octylphenyl ether, polyoxyalkylene nonylphenyl ether, polyoxyalkyldibutylphenyl ether, polyoxyalkyl styrylphenyl ether, polyoxyalkyl benzylphenyl ether, polyoxyalkylbisphenyl ether, polyoxyalkylcumylphenyl ether, and polyoxyalkylene phenyl ether. As nonionic surfactants, ionic surfactants having aromatic rings (so-called aromatic nonionic surfactants) are preferred, polyoxyalkylene phenyl ether is more preferred, and polyoxyethylene phenyl ether is even more preferred. Aromatic nonionic surfactants tend to have excellent dispersibility, dispersion stability, and high concentration properties for CNT aggregates.

[0136] Other dispersants that excel in dispersibility, dispersion stability, and high concentration of CNTs include: Demol (registered trademark: hereinafter the same) N, Demol RN, and Demol T (manufactured by Kao Corporation), sodium salt of β-naphthalene sulfonic acid formalin condensate; Brij S 100 (manufactured by Sigma-Aldrich), polyoxyethylene stearyl ether; polyvinylpyrrolidone K30 (e.g., manufactured by Fujifilm Wako Pure Chemical Industries, Ltd.); carboxymethylcellulose (CMC) (e.g., manufactured by Daicel Mirise Co., Ltd.); sodium deoxycholate (e.g., manufactured by Fujifilm Wako Pure Chemical Industries, Ltd.); and SOLSPERSE. ＴＭ W100, SOLSPERSE ＴＭ Examples include W150 (manufactured by Lubrizol Japan Co., Ltd.). CMC is particularly preferred from the viewpoint of excellent dispersion ability, dispersion stability, and high concentration of CNT aggregates.

[0137] When the CNT dispersion contains a dispersant, the amount of dispersant used is not particularly limited and can be set appropriately depending on the type of dispersant, the amount of CNT aggregate, the amount of dispersion medium, etc.

[0138] [Method for Manufacturing CNT Dispersion] The method for manufacturing a CNT dispersion is not particularly limited. A CNT dispersion can be manufactured by dispersing CNT aggregates in a dispersion medium. That is, a CNT dispersion can be manufactured by a method that includes a step of dispersing CNT aggregates in a dispersion medium (also called the "dispersion step"). The dispersion mediums that can be used in the dispersion step are as described above.

[0139] The dispersion method is not particularly limited. Examples of dispersion methods include using dispersion devices such as stirrers, homogenizers, colloid mills, flow jet mixers, dissolvers, paint conditioners, Manton emulsifiers, jet mills, and ultrasonic devices. Other examples of dispersion methods include using known grinding means, such as ball milling (e.g., ball mills, vibrating ball mills, planetary ball mills, bead mills, etc.), sand milling, colloid milling, jet milling, roller milling, vertical or horizontal agitator mills, attritors, colloid mills, three-roll mills, pearl mills, super mills, impellers, despersers, KD mills, dynatrons, and pressurized kneaders. The method using a jet mill is preferred, and the method using a wet jet mill is more preferred. A wet jet mill is a dispersion device that pumps a mixture in a solvent as a high-speed flow from a nozzle placed in a sealed state inside a pressure vessel. In a wet jet mill, CNT aggregates are dispersed within a pressure vessel by collisions between opposing flows, collisions with the vessel wall, turbulence and shear flow generated by high-speed flow, etc. A suitable wet jet mill is an ultra-high pressure homogenizer manufactured by Jōkō Co., Ltd. (model numbers: NAGS20, NAGS100, JAGS200, NAGS1000, etc.). However, the wet jet mill is not limited to these. When using the above-mentioned ultra-high pressure homogenizer as the dispersion device, the dispersion processing pressure is preferably 10 MPa to 250 MPa.

[0140] The method for producing a CNT dispersion may include a step of drying the CNT aggregate (also called a "drying step") before the dispersion step described above.

[0141] If moisture adheres to the CNTs, the surface tension of the water can cause the CNTs to stick together, raising concerns about reduced dispersibility. Therefore, by performing a drying step of the conductive additive before the dispersion step, moisture adhering to the CNTs is removed, preventing the CNTs from sticking together due to moisture, and further improving the dispersibility of the CNTs in the dispersion medium. The drying method is not particularly limited. Examples of drying methods include heating drying, vacuum drying, and heating vacuum drying. Heating vacuum drying is preferred as the drying method. The drying temperature is not particularly limited, but is preferably, for example, 40°C to 100°C. The drying time is not particularly limited and can be set appropriately depending on the drying temperature, the degree of moisture adhering to the CNT aggregate in this disclosure, etc.

[0142] The following are examples of CNT dispersion manufacturing methods, but the manufacturing of CNT dispersions is not limited to those shown below.

[0143] <Manufacturing Example 1: Example of Dispersion Production> 0.040 g of the CNT aggregate according to this disclosure is weighed and placed in a three-necked flask. After adding the CNT aggregate, a large excess of deionized water, which is the dispersion medium, is poured into the flask (for example, 20 mL), and the mixture is stirred at room temperature (25°C, the same applies hereafter). At this time, a known dispersant (for example, carboxymethylcellulose) may be added as appropriate. Next, the conductive additive is dispersed in the dispersion medium using a known dispersion device (for example, an ultrasonic irradiation device or a wet jet mill). The obtained dispersion is further stirred with a stirrer at room temperature for a long time (for example, 1 hour to 48 hours). In this way, a CNT dispersion is obtained.

[0144] [Conductive Material] The conductive material according to this disclosure includes a CNT aggregate. As described above, the CNT aggregate contained in the conductive material according to this disclosure has excellent conductivity when dispersed, and is therefore suitable as a conductive additive. Because the conductive material according to this disclosure includes the CNT aggregate according to this disclosure, it has excellent conductivity efficiency and can effectively impart high conductivity to the object to be used.

[0145] The conductive material relating to this disclosure may contain known conductive additives such as graphite and Ketjenblack. Furthermore, the conductive material relating to this disclosure may contain CNTs other than specific CNT aggregates.

[0146] The conductive material relating to this disclosure can be used as one of the electrode materials. An example of an electrode formed using the electrode material is an electrode provided in a secondary battery. An embodiment of an electrode and a secondary battery equipped with the electrode will be described below.

[0147] <Electrode> The electrode according to this disclosure includes an electrode active material and a conductive material according to this disclosure. Because the electrode according to this disclosure includes a conductive material according to this disclosure, it has excellent conductivity for forming conductive paths within the electrode. Therefore, the secondary battery according to this disclosure has excellent cycle characteristics.

[0148] In electrodes, CNT aggregates can function as conductive additives. The CNT aggregates included in the electrodes described below are synonymous with the CNT aggregates in this disclosure, and the preferred embodiments are also the same; therefore, a description of the CNT aggregates will be omitted below.

[0149] The electrode may consist of at least one of a positive electrode and a negative electrode. The electrode may include an electrode active material layer, or it may include a current collector and an electrode active material layer disposed on the current collector.

[0150] The current collector is not particularly limited as long as it does not induce chemical changes in the battery and is conductive. Examples of current collectors include copper, stainless steel, aluminum, nickel, titanium, calcined carbon, and aluminum or stainless steel surfaces that have been surface-treated with carbon, nickel, titanium, silver, etc. Specifically, transition metals with good carbon adsorption properties, such as copper and nickel, may be used as current collectors.

[0151] The electrode active material layer can contain an electrode active material. The electrode active material is preferably electrode active material particles. When the electrode is a positive electrode, the electrode active material is not particularly limited, and the electrode active material layer can contain a positive electrode active material commonly used in positive electrode materials for electrodes. Specifically, examples of the positive electrode active material include layered compounds such as lithium cobalt oxide (LiCoO ２ ), lithium nickel oxide (LiNiO ２ ), etc., compounds substituted with one or more transition metals; lithium iron oxides such as LiFe ３ O ４ ; lithium manganese oxides represented by chemical formulas Li １＋ｃ１ Mn ２－ｃ１ O ４ (0 ≦ c1 ≦ 0.33), LiMnO ３ , LiMn ２ O ３ , LiMnO ２ , etc.; lithium copper oxide (Li ２ CuO ２ ); vanadium oxides such as LiV ３ O ８ , V ２ O ５ , Cu ２ V ２ O ７ ; Ni-site type lithium nickel oxides represented by the chemical formula LiNi １－ｃ２ M ｃ２ O ２ (where M is at least one selected from the group consisting of Co, Mn, Al, Cu, Fe, Mg, B, and Ga, and satisfies 0.01 ≦ c2 ≦ 0.66); lithium manganese composite oxides represented by the chemical formula LiMn ２－ｃ３ M ｃ３ O ２ (where M is at least one selected from the group consisting of Co, Ni, Fe, Cr, Zn, and Ta, and satisfies 0.01 ≦ c3 ≦ 0.1), or Li ２ Mn ３ MO ８ (where M is at least one selected from the group consisting of Fe, Co, Ni, Cu, and Zn); lithium manganese oxides in which part of the Li in the chemical formula is substituted with alkaline earth metal ions, LiMn ２ O ４These are some examples.

[0152] When the electrode is a negative electrode, the electrode active material is not particularly limited, and the electrode active material layer may include negative electrode active materials commonly used for negative electrode materials. Specifically, the negative electrode active material may include graphite-based active material particles or silicon-based active material particles. As graphite-based active material particles, at least one selected from the group consisting of artificial graphite, natural graphite, graphitized carbon fiber, and graphitized mesocarbon microbeads may be used. By using artificial graphite as graphite-based active material particles, rate characteristics can be improved. As silicon-based active material particles, at least one selected from the group consisting of Si, SiOx (0 < x < 2), Si-C composite, and Si-Y alloy (where Y is an element selected from the group consisting of alkali metals, alkaline earth metals, transition metals, group 13 elements, group 14 elements, rare earth elements, and combinations thereof) may be used. By using silicon-based active material particles, the battery capacity can be increased.

[0153] The electrode active material layer may further contain a binder. The binder is not particularly limited, and the electrode active material layer may include binders commonly used in electrode materials. Examples of binders include at least one polymer selected from the group consisting of polyvinylidene fluoride-hexafluoropropylene copolymer (PVDF-co-HFP), polyvinylidene fluoride, polyacrylonitrile, polymethyl methacrylate, polyvinyl alcohol, carboxymethylcellulose (CMC), starch, hydroxypropylcellulose, regenerated cellulose, polyvinylpyrrolidone, tetrafluoroethylene, polyethylene, polypropylene, ethylene propylene diene monomer (EPDM), sulfonated EPDM, styrene-butadiene rubber (SBR), fluororubber, and polyacrylic acid, as well as polymers in which the hydrogen atoms of these polymers are substituted with Li, Na, Ca, etc.

[0154] <Secondary Battery> The secondary battery according to this disclosure comprises electrodes according to this disclosure. The secondary battery may include a negative electrode, a positive electrode, a separator interposed between the positive electrode and the negative electrode, and an electrolyte. At least one of the positive electrode and the negative electrode is an electrode according to this disclosure.

[0155] A separator separates the negative electrode from the positive electrode and provides a passage for lithium ions to move. It is generally not limited to any separator commonly used in secondary batteries. Preferably, the separator has low resistance to ion movement in the electrolyte and excellent electrolyte moisture absorption capacity. Specifically, a porous polymer film can be used as a separator. The porous polymer film may be, for example, a porous polymer film made from polyolefin polymers such as ethylene homopolymer, propylene homopolymer, ethylene / butene copolymer, ethylene / hexene copolymer, or ethylene / methacrylate copolymer, or a laminated structure in which two or more of these films are laminated. Alternatively, the separator may be a conventional porous nonwoven fabric, such as a nonwoven fabric made of high-melting-point glass fibers or polyethylene terephthalate fibers. Furthermore, the separator may be coated with a ceramic component or polymer substance to ensure heat resistance or mechanical strength. The separator can selectively have a single-layer or multi-layer structure.

[0156] The electrolyte is not particularly limited and can include, for example, organic liquid electrolytes, inorganic liquid electrolytes, solid polymer electrolytes, gel-type polymer electrolytes, solid inorganic electrolytes, and molten inorganic electrolytes that can be used in the manufacture of lithium secondary batteries.

[0157] Specifically, the electrolyte may include non-aqueous organic solvents and metal salts. Examples of non-aqueous organic solvents include N-methyl-2-pyrrolidinone, propylene carbonate, ethylene carbonate, butylene carbonate, dimethyl carbonate, diethyl carbonate, γ-butyrolactone, 1,2-dimethoxyethane, tetrahydroxyfuran, 2-methyltetrahydrofuran, dimethyl sulfoxide, 1,3-dioxolane, formamide, dimethylformamide, dioxolane, acetonitrile, nitromethane, methyl formate, methyl acetate, triester phosphate, trimethoxymethane, dioxolane derivatives, sulfolane, methylsulfolane, 1,3-dimethyl-2-imidazolidinone, propylene carbonate derivatives, tetrahydrofuran derivatives, ethers, methyl propionate, and ethyl propionate, which are aprotic organic solvents.

[0158] Among carbonate-based organic solvents, cyclic carbonates such as ethylene carbonate and propylene carbonate are preferred as non-aqueous organic solvents because they have high dielectric constants as high-viscosity organic solvents and readily dissociate lithium salts. It is even more preferable to use a mixture of such cyclic carbonates with low-viscosity, low-dielectric-constant linear carbonates such as dimethyl carbonate and diethyl carbonate in appropriate proportions as a non-aqueous organic solvent, as this yields an electrolyte with high electrical conductivity.

[0159] The metal salt may also be a lithium salt. Lithium salts are readily soluble in non-aqueous electrolytes. For example, the anion portion of the lithium salt may be F － , Cl － , I － NO ３ － , N (CN) ２ － BF ４ － , ClO ４ － , PF ６ － (CF ３ ) ２ PF ４ － (CF３ ) ３ PF ３ － 、(CF ３ ) ４ PF ２ － 、(CF ３ ) ５ PF － 、(CF ３ ) ６ P － 、CF ３ SO ３ － 、CF ３ CF ２ SO ３ － 、(CF ３ SO ２ ) ２ N － 、(FSO ２ ) ２ N － 、CF ３ CF ２ (CF ３ ) ２ CO － 、(CF ３ SO ２ ) ２ CH － 、(SF ５ ) ３ C － 、(CF ３ SO ２ ) ３ C － 、CF ３ (CF ２ ) ７ SO ３ － 、CF ３ CO ２ － 、CH ３ CO ２ － 、SCN － 、及び、(CF ３ CF<​​​​​​​​​In addition to non-aqueous organic solvents and metal salts, the electrolyte may further contain one or more additives for the purpose of improving battery life characteristics, suppressing the decrease in battery capacity, and improving battery discharge capacity, such as haloalkylene carbonate compounds like difluoroethylene carbonate, pyridine, triethyl phosphite, triethanolamine, cyclic ethers, ethylenediamine, n-glycemic (glyme), hexalic acid triamide, nitrobenzene derivatives, sulfur, quinone imine dyes, N-substituted oxazolidinone, N,N-substituted imidazolidine, ethylene glycol dialkyl ether, ammonium salts, pyrrole, 2-methoxyethanol, and aluminum trichloride.

[0161] The secondary battery described above can constitute a battery module containing the secondary battery as a unit cell, and a battery pack containing the battery module. The battery module and battery pack can be used as a power source for medium to large devices selected from the group consisting of electric vehicles, hybrid electric vehicles, plug-in hybrid electric vehicles, and power storage systems.

[0162] <Planar Assembly> The planar assembly relating to this disclosure includes the CNT assembly relating to this disclosure. The proportion of the CNT assembly relating to this disclosure contained in the planar assembly relating to this disclosure is usually 1% by mass or more with respect to the total mass of the planar assembly. The planar assembly relating to this disclosure may contain components other than the CNT assembly relating to this disclosure.

[0163] Examples of planar aggregates relating to this disclosure include films containing the CNT aggregate relating to this disclosure.

[0164] The planar assemblies relating to this disclosure are useful, for example, in filters, electromagnetic shields, and pellicles for extreme ultraviolet (EUV) radiation.

[0165] The method for producing the planar aggregate according to this disclosure is not particularly limited. The planar aggregate according to this disclosure can be produced, for example, as a nonwoven fabric-like planar aggregate by dispersing the CNT aggregate according to this disclosure in water or other fluid and filtering it once or twice or more.

[0166] The planar assemblies relating to this disclosure are useful, for example, in filters, electromagnetic shields, and pellicles for extreme ultraviolet (EUV) applications.

[0167] <Laminate> The laminate according to this disclosure comprises a substrate and a planar assembly according to this disclosure. The substrate and the planar assembly may be in direct contact, or other layers may be arranged between the substrate and the planar assembly. Alternatively, the planar assembly according to this disclosure may be arranged on the substrate, and yet another layer may be arranged on the planar assembly.

[0168] The material constituting the substrate may be resin, glass, or fiber. Examples of resins include polyethylene terephthalate (PET), polycarbonate (PC), polymethyl methacrylate (PMMA), cyclic olefin polymer (COP), triacetate (TAC), cyclic olefin copolymer (COC), poly(vinyl chloride) (PVC), poly(ethylene 2,6-naphthalate) (PEN), polyimide (PI), polypropylene (PP), polyethylene (PE), polystyrene (PS), polyamide (PA), polyacetal (POM), polyurethane (PU), acrylonitrile butadiene styrene (ABS), polyacetal (POM), polyphenylene ether (PPS), polysulfone (PSU), polyether ether ketone (PEEK), and polyamide-imide (PAI). Examples of glass include float glass (SiO2). ２ Na ２ Examples include sodium chloride (containing O, CaO, and MgO), soda lime, aluminosilicate glass, and borosilicate glass. Examples of fibers include synthetic fibers such as polyester fibers, polyamide fibers, polyolefin fibers, and acrylic fibers; and natural fibers such as cotton, linen, silk, wool, cashmere, mohair, alpaca, jute, hemp, and ramie.

[0169] The planar aggregate preferably contains a binder in addition to the CNT aggregate according to this disclosure. The binder is preferably a polymer and preferably contains at least one selected from the group consisting of polymers containing constituent units derived from vinylidene chloride (e.g., polyvinylidene chloride, vinylidene chloride-vinyl chloride copolymer, vinylidene chloride-vinyl acetate copolymer, etc.), polyimide, polysiloxane, and epoxy resin.

[0170] The following examples will provide a more detailed explanation of the CNT aggregates, etc., related to this disclosure. This disclosure is not limited to the following examples, unless it exceeds the spirit of the disclosure.

[0171] (Example 1) 1. Production of Sheet-Shaped CNT Assembly 1 Sheet-shaped CNT assembly 1 was produced by a floating catalyst method (CVD method) in which the self-assembly of CNT bundles directly interacts with the catalyst in the gas phase. A cylindrical reactor with an inner diameter of 85 mm was used as the CNT reactor. First, ferrocene, as a metal catalyst precursor containing Fe atoms, and thiophene, as an accelerator, were introduced into a continuous flow of carrier gas in a once-through reactor whose temperature was controlled to 200°C to 800°C. Hydrogen gas was used as the carrier gas. By maintaining the temperature in the once-through reactor within the above range, the metal catalyst precursor decomposes. The region in which the metal catalyst precursor decomposes is referred to as the first temperature zone.

[0172] Next, methane, the carbon source, was released into the carrier gas stream. The metal catalyst and carbon source were supplied to a second temperature zone, temperature-controlled at 1400°C, located downstream of the first temperature zone. The total gas supply flow rate for the carrier gas and source gas was set to 34 NL / min (NL is normal liters). The second temperature zone was maintained at a temperature sufficient to generate carbon nanotube aggregates.

[0173] In the second temperature zone, a reaction field was generated within the temperature-controlled flow reactor, forming catalytic nuclei and causing rapid growth of CNTs, thereby generating CNT aggregates. The aggregates were discharged as continuous discharge through the outlet of the flow-type reactor, which was temperature-controlled between 200°C and 700°C, and sheet-like CNT aggregates were collected. The obtained sheet-like CNT aggregates were washed with pure water for 10 seconds, crushed into a powder, and then passed through a sieve with a mesh size of 1.0 mm twice. The CNT aggregates that passed through the sieve were collected and designated as CNT aggregate 1.

[0174] <Evaluation of CNT aggregates 1: Na atom content> The Na atom content relative to the total mass of CNT aggregate 1 was measured using an inductively coupled plasma mass spectrometer (ICP-MS) (PerkinElmer, NexION 2000C). The sheet-like CNT aggregate 1 obtained above was pretreated by low-temperature ashing / acid dissolution and then measured using the above apparatus. The Na atom content in CNT aggregate 1 was 90 ppm by mass. The evaluation results are shown in Table 1.

[0175] <Evaluation of CNT aggregate 2: Measurement of cumulative 50% particle size D50 in volume-based particle size distribution> Using CNT aggregate 1, CNT dispersion 1 was prepared according to "2. Preparation of CNT dispersion 1" described later. CNT dispersion 1 was thoroughly stirred and then diluted with pure water. The obtained diluted solution was used as a sample, and the cumulative particle size D50 of the CNT dispersion was measured using a particle size analyzer (LA-960, laser diffraction particle size analyzer, Horiba, Ltd.). The particle refractive index of CNTs was set to 1.920-0.522i. The refractive index of the solvent was set to 1.333. During measurement, CNT dispersion 1 was diluted by dropping it into pure water while observing the transmittance, and the measurement was performed after confirming that the particle size distribution on the monitor was stable. As a result, the cumulative 50% particle size D50 in the volume-based particle size distribution of CNT aggregate 1 was 12.53 μm. The evaluation results are shown in Table 1.

[0176] 2. Preparation of CNT dispersion 1 The following materials were mixed and pre-dispersed by treating them with an Ace homogenizer manufactured by Nippon Seiki Co., Ltd. for 1 hour to obtain pre-dispersion 1.

[0177] (Dispersion composition) - CNT aggregate 1 obtained above... 1.1 g - CARBOXYMETHYL CELLULOSE SODIUM SALT HIGH VISCOSITY (manufactured by MP Biomedicals)... 1.65 g - Purified water... 547.25 g

[0178] The main dispersion of pre-dispersion 1 was carried out using a high-pressure homogenizer (model number: NAGS100) manufactured by Jōkō Co., Ltd. as a wet jet mill under the following conditions, and a CNT dispersion 1 was obtained in which the concentration of CNT aggregates was 0.20% by mass and the concentration of sodium carboxymethylcellulose was 0.30% by mass. (Dispersion conditions) Nozzle diameter: 0.22 mm Pressure: 85 MPa Number of cycles: 8 Method: Circulation method

[0179] <Evaluation of CNT dispersion 1: Viscosity> The viscosity of CNT dispersion 1 was measured using a cone-plate viscometer (also known as an E-type viscometer). Specifically, a cone-plate viscometer (BROOKFIELD DV-II+Pro PROGRAMMABLE VISCOMETER) was used to measure the viscosity. Measurement fixture: Cone plate Measurement mode: Rotation mode Shear rate: 0.6 s －１ ~384 simultaneous －１ Temperature: 25°C. From the obtained data, the shear rate was 12 s. －１ The viscosity was measured. The viscosity of the dispersion was 434.0 mPa·s. The results are shown in Table 1.

[0180] <Evaluation of CNT dispersion 1: Elongation at break> CNT dispersion 1 was poured onto a 22 mm x 75 mm x 3 mm slide glass type silicon plate (manufactured by Dosaka E-M Co., Ltd., #08-1044), heated at 100°C for 30 minutes and dried to prepare the sample for measurement. The sample for measurement was fixed to the gripping part of a tensile testing apparatus (manufactured by Shimadzu Corporation, Autograph AG-IS), and a tensile test was performed at a speed of 1 mm / min. The point at which the test force was maximum was considered the breaking point, and the elongation at break was calculated. As a result, the elongation at break was 1.5%.

[0181] <Evaluation of CNT dispersion 1: Surface resistivity> CNT dispersion 1 was poured onto a 22 mm x 75 mm x 3 mm slide glass type silicon plate (manufactured by Dosaka E-M Co., Ltd., #08-1044), heated to 100°C, and dried for 30 minutes to be used as the measurement sample. The surface resistivity of the film was measured using a Loresta GXII manufactured by Nitto Seiko Analytech Co., Ltd. Measurements were taken at five locations on the film, and the average of the five values ​​was taken as the surface resistivity. As a result, the surface resistivity was 1.14 Ω / □. The results are shown in Table 1.

[0182] (Example 2) 1. Manufacturing of CNT Assembly 2 CNT assembly 2 was manufactured by mixing CNT assembly 2A and CNT assembly 2B described below. CNT assembly 2A was manufactured in the same manner as CNT assembly 1, except that the total gas supply flow rate of the carrier gas and raw material gas was set to 35 NL / min. CNT assembly 2B was manufactured in the same manner as CNT assembly 1, except that the total gas supply flow rate of the carrier gas and raw material gas was set to 36 NL / min.

[0183] <Evaluation of CNT Assembly 2 1: Na Atom Content> The amount of Na atoms relative to the total mass of CNT assembly 2 was measured in the same manner as in Example 1. The amount of Na atoms contained in CNT assembly 2 was 20 ppm by mass. The evaluation results are shown in Table 1.

[0184] <Evaluation of CNT aggregate 2: Measurement of cumulative 50% particle size D50 in volume-based particle size distribution> Using CNT aggregate 2, CNT dispersion 2 was prepared according to "2. Preparation of CNT dispersion 2" described later. For CNT dispersion 2, the cumulative 50% particle size D50 in volume-based particle size distribution was measured in the same manner as in Example 1. As a result, the cumulative 50% particle size D50 in volume-based particle size distribution of CNT aggregate 2 was 7.67 μm. The evaluation results are shown in Table 1.

[0185] 2. Preparation of CNT dispersion 2 Using the obtained CNT aggregate 2, a CNT dispersion 2 was obtained in the same manner as in Example 1.

[0186] <Evaluation of CNT dispersion 2: Viscosity> The viscosity of CNT dispersion 2 was measured using the same method as in Example 1. The viscosity of the dispersion was 282.1 mPa·s. The results are shown in Table 1.

[0187] <Evaluation of CNT dispersion 2: Elongation at break> The elongation at break was calculated using CNT dispersion 2 in the same manner as in Example 1. As a result, the elongation at break was 2.0%.

[0188] <Evaluation of CNT dispersion 2: Surface resistivity> The surface resistivity of the film was measured using CNT dispersion 2 in the same manner as in Example 1. Measurements were taken at five locations on the film, and the average of the five values ​​was taken as the surface resistivity. As a result, the surface resistivity was 1.24 Ω / □. The results are shown in Table 1.

[0189] (Example 3) 1. Manufacturing of sheet-like CNT aggregate 3 The sheet-like CNT aggregate 3 was manufactured by the same method as in Example 2.

[0190] <Evaluation of CNT Assembly 3 1: Na Atom Content> The amount of Na atoms relative to the total mass of CNT assembly 3 was measured in the same manner as in Example 1. The amount of Na atoms contained in CNT assembly 3 was 20 ppm by mass. The evaluation results are shown in Table 1.

[0191] <Evaluation of CNT aggregate 2: Measurement of cumulative 50% particle size D50 in volume-based particle size distribution> Using CNT aggregate 3, CNT dispersion 3 was prepared according to "2. Preparation of CNT dispersion 3" described later. For CNT dispersion 3, the cumulative 50% particle size D50 in volume-based particle size distribution was measured in the same manner as in Example 1. As a result, the cumulative 50% particle size D50 in volume-based particle size distribution of CNT aggregate 3 was 13.05 μm. The evaluation results are shown in Table 1.

[0192] 2. Preparation of CNT dispersion 3 A pre-dispersion 3 was obtained using the obtained CNT aggregate 3 in the same manner as in Example 1.

[0193] CNT dispersion 3 was obtained in the same manner as in Example 1, except that the main dispersion of the pre-dispersion 3 was carried out using a super-high pressure homogenizer (model number: NAGS100) manufactured by Jōkō Co., Ltd. as a wet jet mill under the following conditions. (Dispersion conditions) Nozzle diameter: 0.22 mm Pressure: 50 MPa Number of passes: 3 Method: Circulation method

[0194] <Evaluation of CNT dispersion 3: Viscosity> The viscosity of CNT dispersion 3 was measured using the same method as in Example 1. The viscosity of the dispersion was 798.2 mPa·s. The results are shown in Table 1.

[0195] <Evaluation of CNT dispersion 3: Elongation at break> The elongation at break was calculated using CNT dispersion 3 in the same manner as in Example 1. As a result, the elongation at break was 2.6%.

[0196] <Evaluation of CNT dispersion 3: Surface resistivity> The surface resistivity of the film was measured using CNT dispersion 3 in the same manner as in Example 1. Measurements were taken at five locations on the film, and the average of the five values ​​was taken as the surface resistivity. As a result, the surface resistivity was 0.90 Ω / □. The results are shown in Table 1.

[0197] (Example 4) 1. Manufacturing of sheet-like CNT aggregate 4 CNT aggregate 4 was manufactured in the same manner as CNT aggregate 1, except that the total gas supply flow rate of the carrier gas and raw material gas was set to 17 NL / min.

[0198] <Evaluation of CNT Assembly 4 1: Na Atom Content> The Na atom content relative to the total mass of CNT assembly 4 was measured in the same manner as in Example 1. The amount of Na atoms contained in CNT assembly 4 was 100 ppm by mass. The evaluation results are shown in Table 1.

[0199] <Evaluation of CNT aggregate 4 2: Measurement of cumulative 50% particle size D50 in volume-based particle size distribution> Using CNT aggregate 4, CNT dispersion 4 was prepared according to "2. Preparation of CNT dispersion 4" described later. For CNT dispersion 4, the cumulative 50% particle size D50 in volume-based particle size distribution was measured in the same manner as in Example 1. As a result, the cumulative 50% particle size D50 in volume-based particle size distribution of CNT aggregate 4 was 1.18 μm. The evaluation results are shown in Table 1.

[0200] 2. Preparation of CNT dispersion 4 A pre-dispersion 4 was obtained using the obtained CNT aggregate 4 in the same manner as in Example 1.

[0201] The pre-dispersion 4 was subjected to the final dispersion using a high-pressure homogenizer (model number: NAGS100) manufactured by Jōkō Co., Ltd. as a wet jet mill under the following conditions to obtain the CNT dispersion 4. (Dispersion conditions) Nozzle diameter: 0.22 mm Pressure: 150 MPa Number of passes: 8 Method: Circulation method

[0202] <Evaluation of CNT dispersion 4: Viscosity> The viscosity of CNT dispersion 4 was measured using the same method as in Example 1. The viscosity of the dispersion was 292.9 mPa·s. The results are shown in Table 1.

[0203] <Evaluation of CNT dispersion 4: Elongation at break> The elongation at break was calculated using CNT dispersion 4 in the same manner as in Example 1. As a result, the elongation at break was 2.8%.

[0204] <Evaluation of CNT dispersion 4: Surface resistivity> The surface resistivity of the film was measured using CNT dispersion 4 in the same manner as in Example 1. Measurements were taken at five locations on the film, and the average of the five values ​​was taken as the surface resistivity. As a result, the surface resistivity was 2.85 Ω / □. The results are shown in Table 1.

[0205] (Comparative Example 1) 1. Preparation of Powdered CNT Assembly 5 As the powdered CNT assembly 5, carbon nanotubes manufactured by C-nano Co., Ltd. (catalog number: FT6120) were prepared.

[0206] <Evaluation of CNT aggregate 1: Na atom content> The Na atom content relative to the total mass of CNT aggregate 5 was measured in the same manner as in Example 1. The amount of Na atoms contained in CNT aggregate 5 was 60 ppm by mass. The evaluation results are shown in Table 1.

[0207] <Evaluation of CNT aggregate 2: Measurement of cumulative 50% particle size D50 in volume-based particle size distribution> Using the CNT aggregate 5, a CNT dispersion 5 was prepared according to "2. Preparation of CNT dispersion 5" described later. For the CNT dispersion 5, the cumulative 50% particle size D50 in volume-based particle size distribution was measured in the same manner as in Example 1. As a result, the cumulative 50% particle size D50 in volume-based particle size distribution of the CNT aggregate 5 was 0.48 μm. The evaluation results are shown in Table 1.

[0208] 2. Preparation of CNT dispersion 5: Using the prepared powdered CNT aggregate 5, a CNT dispersion 5 was obtained in the same manner as in Example 1.

[0209] <Evaluation of CNT dispersion 5: Viscosity> The viscosity of CNT dispersion 5 was measured using the same method as in Example 1. The viscosity of the dispersion was 9.3 mPa·s. The results are shown in Table 1.

[0210] <Evaluation of CNT dispersion 5: Elongation at break> The elongation at break was calculated using CNT dispersion 5 in the same manner as in Example 1. As a result, the elongation at break was 3.7%.

[0211] <Evaluation of CNT dispersion 5: Surface resistivity> The surface resistivity of the film was measured using CNT dispersion 5 in the same manner as in Example 1. Measurements were taken at five locations on the film, and the average of the five values ​​was taken as the surface resistivity. As a result, the surface resistivity was 21.29 Ω / □. The results are shown in Table 1.

[0212] (Comparative Example 2) 1. Preparation of Powdered CNT Assembly 6 As the powdered CNT assembly 6, carbon nanotubes manufactured by C-nano Co., Ltd. (catalog number: FT7000) were prepared.

[0213] <Evaluation of CNT aggregate 1: Na atom content> The Na atom content relative to the total mass of CNT aggregate 6 was measured in the same manner as in Example 1. The amount of Na atoms contained in CNT aggregate 6 was 200 ppm by mass. The evaluation results are shown in Table 1.

[0214] <Evaluation of CNT aggregate 2: Measurement of cumulative 50% particle size D50 in volume-based particle size distribution> Using the CNT aggregate 6, a CNT dispersion 6 was prepared according to "2. Preparation of CNT dispersion 6" described later. For the CNT dispersion 6, the cumulative 50% particle size D50 in volume-based particle size distribution was measured in the same manner as in Example 1. As a result, the cumulative 50% particle size D50 in volume-based particle size distribution of the CNT aggregate 6 was 0.65 μm. The evaluation results are shown in Table 1.

[0215] 2. Preparation of CNT dispersion 6: Using the prepared powdered CNT aggregate 6, a CNT dispersion 5 was obtained in the same manner as in Example 1.

[0216] <Evaluation of CNT dispersion 6: Viscosity> The viscosity of CNT dispersion 6 was measured using the same method as in Example 1. The viscosity of the dispersion was 6.4 mPa·s. The results are shown in Table 1.

[0217] <Evaluation of CNT dispersion 6: Elongation at break> The elongation at break was calculated using CNT dispersion 6 in the same manner as in Example 1. As a result, the elongation at break was 2.6%.

[0218] <Evaluation of CNT dispersion 6: Surface resistivity> The surface resistivity of the film was measured using CNT dispersion 6 in the same manner as in Example 1. Measurements were taken at five locations on the film, and the average of the five values ​​was taken as the surface resistivity. As a result, the surface resistivity was 16.52 Ω / □. The results are shown in Table 1.

[0219] Next, we fabricated a lithium-ion secondary battery.

[0220] 1. Fabrication of positive electrode for lithium secondary battery: Positive electrode active material (LiNi ０．８ Co ０．１ Mn ０．１ O ２A positive electrode mixture was prepared by mixing a conductive material (acetylene black) and a binder (PVdF) in a ratio of positive electrode active material:conductive material:binder = 92:5:3 (mass ratio), and then kneading with N-methyl-2-pyrrolidone. The obtained positive electrode mixture was applied to a 15 μm thick Al foil to be used as a current collector, vacuum-dried at 80°C for 1 hour, and then roll-pressed to obtain a positive electrode for a lithium secondary battery. The positive electrode area was 1.65 cm², and the basis weight was 16 mg / cm². ２ The density is 3.0 g / cm³. ３ It was prepared to achieve the following result.

[0221] 2. Preparation of a Negative Electrode for Lithium Secondary Batteries A negative electrode for lithium secondary batteries was prepared by mixing artificial graphite MAG-E and carbon-coated SiO in a 9:1 (mass ratio) ratio as the negative electrode active material, using CLPA-C07 (manufactured by Fujifilm Wako Pure Chemical Industries, Ltd.) as a binder, and adding the CNT dispersion 1 from Example 1 as a conductive additive, so that the composition was negative electrode active material:binder:conductive additive = 94.9:5.0:0.1 (mass ratio), and kneading to prepare a paste-like negative electrode mixture. Ion-exchanged water was used as the solvent during the preparation of the negative electrode mixture. The obtained negative electrode mixture was coated onto a 20 μm thick Cu foil using a single-sided continuous coating machine, dried at 120°C, and then roll-pressed to obtain a negative electrode for lithium secondary batteries. The negative electrode area was 1.77 cm². ２ The estimated amount is 9.3 mg / cm³. ２ The density is 1.4 g / cm³. ３ It was prepared to achieve the following result.

[0222] 3. Fabrication of a Lithium Secondary Battery The positive electrode for the lithium secondary battery was placed on the lower cover of a part for the coin-type battery R2032 (manufactured by Hosen Co., Ltd.), and a laminated film separator, which consists of a 16 μm heat-resistant porous layer laminated on a polyethylene porous film, was placed on top of it. 300 μL of electrolyte was injected into this. As the electrolyte, a 20:75:5 (volume ratio) mixture of ethylene carbonate, dimethyl carbonate, and ethyl methyl carbonate was added, to which 1 volume% of vinylene carbonate was added, and LiPF was added. ６A solution of 1.3 mol / L was used. Next, the negative electrode for the lithium secondary battery was placed on top of the laminated film separator, the top cover was placed on top via a gasket, and the lithium secondary battery of coin-type full cell R2032 was fabricated by crimping with a crimping machine. These operations were performed in a glove box under an argon atmosphere.

[0223] The evaluation results for Examples 1 to 4, Comparative Example 1, and Comparative Example 2 are shown in Table 1.

[0224]

[0225] As shown in Table 1, the CNT dispersions obtained by liquefying the CNT aggregates of Examples 1 to 4 exhibit excellent conductivity and dispersibility. The surface resistivity values ​​for Examples 1 to 4 are 1.14 Ω / □, 1.24 Ω / □, 0.90 Ω / □, and 2.85 Ω / □, respectively, and the viscosity of the dispersions is 434.0 mPa·s, 282.1 mPa·s, 798.2 mPa·s, and 292.9 mPa·s, respectively, which are appropriate values. This confirms that the CNT aggregates of the examples have excellent conductivity and dispersibility. Therefore, the CNT aggregates of Examples 1 to 4 are excellent as conductive materials. On the other hand, the surface resistivity values ​​of the CNT dispersions of Comparative Example 1 and Comparative Example 2 are high, at 21.29 Ω / □ and 16.52 Ω / □, respectively, indicating low conductivity. Furthermore, the viscosities of the dispersions were 9.3 mPa·s and 6.4 mPa·s, respectively, which were too low, resulting in poor handling and making them difficult to use as dispersions, thus resulting in poor workability. These evaluation results indicate that the CNT aggregates of Comparative Example 1 and Comparative Example 2 are inferior as conductive materials.

Claims

1. A carbon nanotube aggregate that satisfies the following conditions (1) and (2): (1) It contains Na atoms, and the Na atom content is less than 200 ppm by mass relative to the total mass of the carbon nanotube aggregate. (2) The elongation at break measured by the following measurement method is greater than 0% and 3.0% or less. (Method for measuring elongation at break) A dispersion with a concentration of 0.20% by mass is prepared by mixing the carbon nanotube aggregate with water. The obtained dispersion is poured onto a 22 mm × 75 mm × 3 mm slide glass type silicon plate, heated at 100°C for 30 minutes to dry and obtain a measurement sample. The obtained measurement sample is fixed to the gripping part of a tensile testing device, and a tensile test is performed at a speed of 1 mm / min. The point where the stress is maximum is considered the breaking point, and the elongation at break is calculated from the length of the measurement sample at the breaking point and the length of the measurement sample before measurement.

2. A carbon nanotube aggregate according to claim 1, satisfying the following condition (3): (3) The cumulative 50% particle size D50 in the volume-based particle size distribution is 1.0 μm or more and 15 μm or less.

3. A conductive material comprising the carbon nanotube aggregate described in claim 1.

4. An electrode comprising an electrode active material and the conductive material described in claim 3.

5. A secondary battery comprising the electrode described in claim 4.

6. A planar aggregate comprising the carbon nanotube aggregate described in claim 1.

7. A laminate comprising a substrate and the planar assembly described in claim 6.

8. A filter using the planar assembly described in claim 6.

9. An electromagnetic shield using the planar assembly described in claim 6.

10. A pellicle for extreme ultraviolet radiation using the planar aggregate described in claim 6.

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