[go: up one dir, main page]

US20100239491A1 - Method of producing carbon nanotubes - Google Patents

Method of producing carbon nanotubes Download PDF

Info

Publication number
US20100239491A1
US20100239491A1 US11/475,919 US47591906A US2010239491A1 US 20100239491 A1 US20100239491 A1 US 20100239491A1 US 47591906 A US47591906 A US 47591906A US 2010239491 A1 US2010239491 A1 US 2010239491A1
Authority
US
United States
Prior art keywords
carbon
catalyst component
cleaning
cylindrical
component
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Abandoned
Application number
US11/475,919
Other languages
English (en)
Inventor
Avetik Harutyunyan
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Honda Motor Co Ltd
Original Assignee
Honda Motor Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Honda Motor Co Ltd filed Critical Honda Motor Co Ltd
Priority to US11/475,919 priority Critical patent/US20100239491A1/en
Assigned to HONDA MOTOR CO., LTD. reassignment HONDA MOTOR CO., LTD. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: HARUTYUNYAN, AVETIK
Priority to JP2009518504A priority patent/JP5358045B2/ja
Priority to PCT/US2007/072098 priority patent/WO2008100325A2/fr
Publication of US20100239491A1 publication Critical patent/US20100239491A1/en
Abandoned legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/74Iron group metals
    • B01J23/745Iron
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/84Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/85Chromium, molybdenum or tungsten
    • B01J23/88Molybdenum
    • B01J23/881Molybdenum and iron
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/90Regeneration or reactivation
    • B01J23/94Regeneration or reactivation of catalysts comprising metals, oxides or hydroxides of the iron group metals or copper
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J38/00Regeneration or reactivation of catalysts, in general
    • B01J38/04Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst
    • B01J38/12Treating with free oxygen-containing gas
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B82NANOTECHNOLOGY
    • B82YSPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
    • B82Y30/00Nanotechnology for materials or surface science, e.g. nanocomposites
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B82NANOTECHNOLOGY
    • B82YSPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
    • B82Y40/00Manufacture or treatment of nanostructures
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B32/00Carbon; Compounds thereof
    • C01B32/15Nano-sized carbon materials
    • C01B32/158Carbon nanotubes
    • C01B32/16Preparation
    • C01B32/162Preparation characterised by catalysts
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J21/00Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/02Boron or aluminium; Oxides or hydroxides thereof
    • B01J21/04Alumina
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J21/00Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/06Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
    • B01J21/08Silica
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/16Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/24Chromium, molybdenum or tungsten
    • B01J23/28Molybdenum
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/40Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
    • B01J23/46Ruthenium, rhodium, osmium or iridium
    • B01J23/462Ruthenium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/74Iron group metals
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02Impregnation, coating or precipitation
    • B01J37/0201Impregnation
    • B01J37/0203Impregnation the impregnation liquid containing organic compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02Impregnation, coating or precipitation
    • B01J37/0234Impregnation and coating simultaneously
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2202/00Structure or properties of carbon nanotubes
    • C01B2202/02Single-walled nanotubes
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2202/00Structure or properties of carbon nanotubes
    • C01B2202/04Nanotubes with a specific amount of walls
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2202/00Structure or properties of carbon nanotubes
    • C01B2202/06Multi-walled nanotubes
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2004/00Particle morphology
    • C01P2004/10Particle morphology extending in one dimension, e.g. needle-like
    • C01P2004/13Nanotubes
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/584Recycling of catalysts

Definitions

  • the present teachings relate to methods of producing carbon nanotubes from initially produced nanotubes so that the subsequently produced nanotubes have the same chirality as the initially produced nanotubes.
  • SWNT single-walled carbon nanotubes
  • Smalley et al. have described a method of “cloning” SWNT grown by a CVD based method by growing SWNT fibers with open ends, reductively docking nanosized transition metal particles to the open ends of the SWNT fibers and restarting growth of the SWNT on the exposed metal particles.
  • the SWNT growth from the docked nanocatalysts is said to have the same diameter and chirality (n,m) as the base SWNT. See Nanoletters , Vol. 5, No. 6, June 2005, pp. 997-1002.
  • the total amount of SWNT that could be grown by prior methods of growing SWNT using metal catalysts was limited by the build-up and coating of the metal catalyst with a layer composed of, among other compounds, amorphous carbon and metal carbides. Additionally, the methods of growing the SWNTs did not offer means of controlling the chirality of the SWNT produced.
  • SWNTs have attracted attention because of their unique chemical and physical properties.
  • a carbon nanotube can be described as a rolled-up graphite sheet in which hexagonal-shaped units of carbon atoms are bound to each other with very strong bonds between the carbon atoms.
  • SWNTs have minimum diameters of about 0.4 nm with lengths ranging as long as several hundred micrometers with extremely small dimensional fluctuations.
  • the electrical conductivity of carbon nanotubes range from a semiconductor to a metal depending upon the chirality of nanotube.
  • Chirality of a nanotube is denoted by a double index (m,m) where n and m are integers that describe how a single strip of hexagonal “chicken-wire” graphite is cut so it forms a tube that wraps perfectly onto the surface of a cylinder.
  • n integers that describe how a single strip of hexagonal “chicken-wire” graphite is cut so it forms a tube that wraps perfectly onto the surface of a cylinder.
  • the resultant tube is said to be of the “arm-chair” (or n,n) type, since when that type of tube is cut perpendicular to the tube axis, only the sides of the hexagons are exposed and their pattern around the periphery of the tube edge resembles the arm and seat of an arm chair repeated n times. Due to their metallic nature, with extremely high electrical and thermal conductivity, the arm-chair tubes are a preferred form of SWNT.
  • Metallic nanotubes can exhibit ballistic conduction, conduction by non-scattered charge carriers. With ballistic conduction, the resistance value becomes independent of length, and the so-called quantum resistance (6.5 k ⁇ ) is observed.
  • Arc discharge, laser ablation, thermal chemical vapor deposition (hereinafter “CVD”) and plasma enhanced CVD are several of the known methods for manufacturing carbon nanotubes. Both SWNT and multi-walled nanotubes can be produced by the arc discharge and laser ablation methods.
  • Catalysts supported on a variety of suitable supports can be utilized in the CVD methods to produce carbon nanotubes.
  • a complete understanding of the effects of catalyst formulation, for instance, transition metals (Ni, Co, Fe, etc.), support material, catalyst/support interaction, synthesis temperature and hydrocarbon gas on the diameter and chirality of the carbon nanotubes produced by CVD methods is still being developed. See, for example, Harutyunyan et al, Nanoletters , Vol. 2, No. 5, 2002, pp. 525-530 and U.S. Patent Application Publication No. US 2003/0124717 A1.
  • the present teachings satisfy the need for a method of producing cylindrical carbon structures from initially produced cylindrical carbon structures so that the subsequently produced cylindrical carbon structures have the same chirality as the initially produced cylindrical carbon structures.
  • a method of preparing cylindrical carbon structures by providing a catalyst component on a substrate and a carbon component, and contacting the catalyst component and the carbon component to produce a first cylindrical carbon structure is taught by the present disclosure.
  • the method further includes stopping providing the carbon component, cleaning the catalyst component, and then again providing the carbon component to produce more of the cylindrical carbon structure.
  • the present teachings further provide single-walled carbon nanotubes prepared by a process including providing a catalyst component on a substrate, providing a carbon component and contacting the catalyst component and the carbon component to produce a first single-walled carbon nanotube having a chirality. Then stopping providing the carbon component, cleaning the catalyst components, and again providing the carbon component to produce a continued first single-walled carbon nanotube, such that the continued first single-walled carbon nanotube has the same chirality as the first single-walled carbon nanotube.
  • Another method disclosed by the present teachings of preparing single-walled carbon nanotubes includes providing a catalyst component on a substrate, providing a carbon component, contacting the catalyst component and the carbon component to produce a first single-walled carbon nanotube having a chirality and stopping providing the carbon component.
  • the catalyst component is then cleaned, and the carbon component is again provided to produce a continued first single-walled carbon nanotube with the same chirality as the first single-walled carbon nanotube. This procedure is repeated until the continued first single-walled carbon nanotube satisfies a desired characteristic, at which time, the single-walled carbon nanotube is removed from the catalyst component.
  • the present teachings provide a method of preparing cylindrical carbon structures, specifically SWNT, by providing a catalyst component on a substrate, providing a carbon component, contacting the catalyst component and the carbon component to produce a first cylindrical carbon structure, and then stopping the provision of the carbon component. At this point in the method, the catalyst component can be cleaned, and after cleaning, the carbon component can be reintroduced to produce additional cylindrical carbon structure.
  • the chirality of the first cylindrical carbon structure can be determined after the provision of the carbon component is stopped.
  • the preparation can then be continued by repeating the steps of providing carbon component, contacting the catalyst and carbon components to produce a continued cylindrical carbon structure, stopping the provision of the carbon component, and cleaning the catalyst component, until the cylindrical carbon structure satisfies a desired characteristic.
  • the chirality of the continued cylindrical carbon structure produced has the same chirality as the first cylindrical carbon structure.
  • the presently disclosed process provides that where given an initial cylindrical carbon structure, preferably an SWNT, with a certain chirality, that cylindrical carbon structure can be, for instance, increased in length with the additional cylindrical carbon structure having the same chirality as the initial cylindrical carbon structure.
  • the desired characteristic can include, for example, at least one member selected from the group consisting of length, electrical conductivity, thermal conductivity, metallic character, semi-conductor character and non-metallic character.
  • the cylindrical carbon structure can be removed from the catalyst component.
  • the production process can be ceased when the efficiency of the process decreases due to build-up of a coating on the catalyst component as described in more detail herein.
  • the catalyst component can include nanoparticles containing at least one member selected from the group consisting of transition metals, such as, for example, iron, nickel, cobalt, molybdenum, ruthenium and combinations thereof.
  • transition metals such as, for example, iron, nickel, cobalt, molybdenum, ruthenium and combinations thereof.
  • catalyst formulations of transition metals and combinations thereof which exhibit resistance to or decreased formation of coatings on the catalyst itself.
  • the coatings are composed of amorphous carbon, multilayer carbon and metal carbides.
  • the present method of producing cylindrical carbon structures can utilize either a plasma enhanced CVD method or a thermal CVD method to produce the carbon component as a carbon vapor produced from a carbon source, such as, for example, methane, ethylene, acetylene or carbon dioxide.
  • a carbon source such as, for example, methane, ethylene, acetylene or carbon dioxide.
  • the catalyst component can be heated to a temperature ranging from about 60° C. to about 100° C.
  • the catalyst nanoparticle utilized in the method can, after exposure for a period of time to a carbon source, develop a coating or layer of non-reactive material.
  • Various cleaning processes are presented in the present disclosure which clean the catalyst component by reducing any coating present on the catalyst component.
  • Cleaning the catalyst component refers to using a cleaning method sufficiently active to remove or deactivate, to the extent that cleaning allows subsequent continued production of the cylindrical carbon structure, any coating or build-up present on the catalyst component.
  • cleaning the catalyst component includes a cleaning method that does not react, or does not react substantially, with the cylindrical carbon structure.
  • Oxidation, reduction, dissolution, radiative heating, chemical treatment, plasma treatment and combinations thereof are examples of suitable cleaning methods for removal of the coating on the catalyst component.
  • chemical treatment include contacting the coating with, for example, water, peroxides and acids.
  • Radiative heating includes exposing the catalyst component and coating to radiation of a wavelength capable of heating primarily the coating and/or the catalyst component to thereby induce oxidation of the coating.
  • the radiative heating does not adversely affect either of the catalyst component or the cylindrical carbon structure.
  • suitable radiation methods include electromagnetic radiation, laser radiation and microwave radiation.
  • the coating present on the catalyst component typically consists of amorphous carbon, multilayer carbon, metal carbide and combinations thereof. According to present theory, without being limited thereby, as the CVD process continues, non-nanotube forming carbon arrives at the catalyst component and can form, for example, amorphous carbon, multilayer carbon and metal carbide. Each of these formations results in decreased access to the catalyst component for the incoming carbon component and eventually leads to decreased or ceased nanotube growth. According to present theory, these coating components arise in a variety of ways, including incomplete combustion of the supplied hydrocarbon, incomplete formation of cylindrical carbon structures, formation of metal carbides with the metallic elements of the catalyst component, and layering of either or both of incompletely combusted hydrocarbons or incompletely formed cylindrical carbon structures.
  • the catalyst component can also become less active through the formation of metal oxides on the catalyst. Reduction of the metal oxides back to the metallic state can also improve the catalyst performance, and can in some cases be accomplished during the cleaning of the catalyst component.
  • the cylindrical carbon structures produced by the present methods can include single-walled carbon nanotubes, double-walled carbon nanotubes and multi-walled carbon nanotubes.
  • the present method produces single-walled carbon nanotubes.
  • the substrate utilized in the presently disclosed methods is not generally restricted, and can include any commonly used substrate. Suitable examples of substrates include, without limitation, silicon substrates, glass substrates, alumina substrates and quartz substrates.
  • single-walled carbon nanotubes can be prepared by providing a catalyst component on a substrate, providing a carbon component and contacting the catalyst component and the carbon component to produce a first single-walled carbon nanotube having a chirality. After a sufficient amount of the initial SWNT is formed, the carbon component is no longer provided, and the catalyst component can be cleaned. After cleaning, the carbon component can again be provided to produce a continued single-walled carbon nanotube which has the same chirality as the first single-walled carbon nanotube.
  • This process can further include determining the chirality of the first single-walled carbon nanotube at any point after the provision of the carbon component has ceased. The process can be repeated until single-walled carbon nanotubes satisfying a desired characteristic are produced, or until the catalyst component after cleaning can no produced the continued first single-walled carbon nanotube.
  • the desired characteristic can be, for instance, length, electrical conductivity, thermal conductivity, metallic character, semi-conductor character and non-metallic character.
  • the present disclosure further includes a process of preparing single-walled carbon nanotubes by providing a catalyst component on a substrate and a carbon component, then contacting the catalyst component and the carbon component to produce a first single-walled carbon nanotube having a chirality. Stopping the provision of the carbon component can be the next step and allows for the cleaning the catalyst component. Repeating the provision of the carbon component and contacting it with the catalyst component produces a continued first single-walled carbon nanotube with the same chirality as the first single-walled carbon nanotube. This process can be repeated until the continued first single-walled carbon nanotube satisfies a desired characteristic, and then removing the single-walled carbon nanotube from the catalyst component.
  • the present process of preparing SWNT can utilize either a plasma enhanced CVD method or a thermal CVD method to produce the carbon component as a carbon vapor produced from a carbon source, such as, for example, methane, ethylene, acetylene or carbon dioxide.
  • a carbon source such as, for example, methane, ethylene, acetylene or carbon dioxide.
  • the catalyst component can be heated to a temperature ranging from about 60° C. to about 100° C.
  • the process can further include determining the chirality of the first produced single-walled carbon nanotube after the provision of the carbon component is ceased.
  • the desired characteristic exhibited by the continued first SWNT can include, for example, length, electrical conductivity, thermal conductivity, metallic character, semi-conductor character and non-metallic character.
  • the catalyst component utilized to produce the SWNT can include nanoparticles which contain transition metals, for instance, iron, nickel, cobalt, molybdenum, ruthenium and combinations thereof.
  • Cleaning the catalyst component can be accomplished by reducing any coating present on the catalyst component.
  • a cleaning method sufficiently active to remove, to the extent that cleaning allows production of the single-walled carbon nanotube, any coating present on the catalyst component is preferable.
  • any cleaning method does not react, or at least does not substantially react, with the single-walled carbon nanotube.
  • oxidation, reduction, dissolution, radiative heating, chemical treatment, plasma treatment and combinations thereof can all be utilized as cleaning methods.
  • Chemical treatment includes contacting the coating with at least one member selected from the group consisting of water, peroxides and acids.
  • Radiative heating includes exposing the coating to, for example, electromagnetic radiation, laser radiation or microwave radiation.
  • the chirality of the cylindrical carbon structures or SWNTs can be determined by a variety of methods including Raman characterization, micro Raman characterization, I-V (“current-voltage”) characterization, and STM (“scanning tunneling microscopy”) measurement.
  • Electromagnetic radiation refers to radiation composed of oscillating electric and magnetic fields and propagated at the speed of light. Examples of electromagnetic radiation include, without limitation, gamma radiation, X-rays, ultraviolet, visible, infrared, microwave and radio waves.
  • Ferric nitrate Fe(NO 3 ) 3 .9H 2 O
  • 2-propanol 2-propanol
  • a previously prepared silicon dioxide substrate can then be immersed into the iron solution for 15 seconds, rinsed in hexane, and dried in air.
  • the substrate with the catalyst can then be placed in a tube furnace and reduced under a helium/hydrogen (60/40) gas flow (200 sccm) at 500 C for one hour.
  • the He/H 2 gas mixture can then be replaced with Ar gas, and the temperature increased to 750 C.
  • methane gas can be added at a flow rate of 20 sccm for 15 minutes, after which time the furnace is cooled to room temperature under a flow of argon.
  • An atomic force microscopy (“AFM”) image can be obtained of the nanotubes.
  • the resulting supported iron nanoparticles with nanotubes can be cleaned by exposing the sample to a dry air flow (100 sccm) at a temperature of 200 C for thirty minutes.
  • the tube furnace can then be reheated to 750 C under a flow (200 sccm) of an argon/hydrogen gas mixture. After the nanoparticles reach a steady state temperature, methane can be re-introduced into the tube furnace, at a flow rate of 20 sccm.
  • the methane flow can be stopped and the apparatus allowed to cool to room temperature under an argon gas flow.
  • the supported iron nanoparticles with nanotubes can then be removed from the tube furnace.
  • a second AFM image can be obtained.
  • the second AFM image can show that the nanotubes have grown in length while maintaining the same chirality as the initial nanotube.
  • Ferric nitrate Fe(NO 3 ) 3 .9H 2 O
  • ammonium molybdate (NH 4 ) 6 Mo 7 O 24 .4H 2 O) at a 1:0.17 Fe:Mo molar ratio
  • the suspension can be deposited, drop wise, onto a previously prepared silicon dioxide substrate, and then dried in air.
  • the substrate with the bimetallic catalyst can then be placed in a tube furnace and reduced under a helium/hydrogen (60/40) gas flow (200 sccm) at 500 C for one hour.
  • the He/H 2 gas mixture can then be replaced with Ar gas, and the temperature increased to 750 C.
  • methane gas can be added at a flow rate of 20 sccm for 15 minutes, after which time the furnace is cooled to room temperature under a flow of argon.
  • An atomic force microscopy (“AFM”) image can be obtained of the nanotubes.
  • the supported iron/molybdenum nanoparticles with nanotubes can be cleaned by exposing the sample to a dry air flow (100 sccm) at a temperature of 200 C for thirty minutes.
  • the tube furnace can then be reheated to 750 C under a flow (200 sccm) of an argon/hydrogen gas mixture. After the nanoparticles reach a steady state temperature, methane can be re-introduced into the tube furnace, at a flow rate of 20 sccm.
  • the methane flow can be stopped and the apparatus allowed to cool to room temperature under an argon gas flow.
  • the supported Fe/Mo nanoparticles with nanotubes can then be removed from the tube furnace.
  • a second AFM image can be obtained.
  • the second AFM image can show that the nanotubes have grown in length while maintaining the same chirality as the initial nanotube.
  • Ferric nitrate Fe(NO 3 ) 3 .9H 2 O
  • methanol can be dissolved in methanol at an approximate concentration of 150 ⁇ g/mL, and then mixed with a methanol suspension of alumina.
  • the alumina can have a BET surface area of 150 m 2 /g.
  • the iron and alumina suspension can be deposited, drop wise, onto a previously prepared silicon dioxide substrate, and then dried in air.
  • the substrate with the catalyst can then be placed in a tube furnace and reduced under a helium/hydrogen (60/40) gas flow (200 sccm) at 500 C for one hour.
  • the He/H 2 gas mixture can then be replaced with Ar gas, and the temperature increased to 750 C.
  • methane gas can be added at a flow rate of 20 sccm for 15 minutes, after which time the furnace is cooled to room temperature under a flow of argon.
  • An atomic force microscopy (“AFM”) image can be obtained of the nanotubes.
  • the supported iron nanoparticles with nanotubes can be cleaned by exposing the sample to a dry air flow (100 sccm) at a temperature of 200 C for thirty minutes.
  • the tube furnace can then be reheated to 750 C under a flow (200 sccm) of an argon/hydrogen gas mixture. After the nanoparticles reach a steady state temperature, methane can be re-introduced into the tube furnace, at a flow rate of 20 sccm.
  • the methane flow can be stopped and the apparatus allowed to cool to room temperature under an argon gas flow.
  • the supported iron nanoparticles with nanotubes can then be removed from the tube furnace.
  • a second AFM image can be obtained.
  • the second AFM image can show that the nanotubes have grown in length while maintaining the same chirality as the initial nanotube.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Nanotechnology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Condensed Matter Physics & Semiconductors (AREA)
  • General Physics & Mathematics (AREA)
  • Physics & Mathematics (AREA)
  • Composite Materials (AREA)
  • Manufacturing & Machinery (AREA)
  • Inorganic Chemistry (AREA)
  • Carbon And Carbon Compounds (AREA)
  • Catalysts (AREA)
US11/475,919 2006-06-28 2006-06-28 Method of producing carbon nanotubes Abandoned US20100239491A1 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
US11/475,919 US20100239491A1 (en) 2006-06-28 2006-06-28 Method of producing carbon nanotubes
JP2009518504A JP5358045B2 (ja) 2006-06-28 2007-06-26 カーボンナノチューブの製造方法
PCT/US2007/072098 WO2008100325A2 (fr) 2006-06-28 2007-06-26 Procédé de production de nanotubes de carbone

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US11/475,919 US20100239491A1 (en) 2006-06-28 2006-06-28 Method of producing carbon nanotubes

Publications (1)

Publication Number Publication Date
US20100239491A1 true US20100239491A1 (en) 2010-09-23

Family

ID=39661384

Family Applications (1)

Application Number Title Priority Date Filing Date
US11/475,919 Abandoned US20100239491A1 (en) 2006-06-28 2006-06-28 Method of producing carbon nanotubes

Country Status (3)

Country Link
US (1) US20100239491A1 (fr)
JP (1) JP5358045B2 (fr)
WO (1) WO2008100325A2 (fr)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20090274609A1 (en) * 2008-05-01 2009-11-05 Honda Motor Co., Ltd. Synthesis Of High Quality Carbon Single-Walled Nanotubes
US20090324484A1 (en) * 2008-05-01 2009-12-31 Honda Motor Co., Ltd. Effect Of Hydrocarbon And Transport Gas Feedstock On Efficiency And Quality Of Grown Single-Walled Nanotubes
US20100081568A1 (en) * 2008-04-21 2010-04-01 Lockheed Martin Corporation Methods for producing carbon nanotubes with controlled chirality and diameter and products therefrom
CN117623287A (zh) * 2023-11-16 2024-03-01 江西铜业技术研究院有限公司 一种高导电碳包覆单壁碳纳米管碳网及制备方法和应用

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BR112012002233A2 (pt) 2009-07-31 2019-09-24 Massachustts Institute Of Tech sietmas e métodos relacionados à formação de nanoestruturas a base de carbono.
FR2949075B1 (fr) 2009-08-17 2013-02-01 Arkema France Catalyseur fe/mo supporte, son procede de preparation et utilisation pour la fabrication de nanotubes
EP2504278A2 (fr) * 2009-11-25 2012-10-03 Massachusetts Institute of Technology Systèmes et procédés d'amélioration de la croissance de nanostructures à base de carbone
WO2012091789A1 (fr) 2010-10-28 2012-07-05 Massachusetts Institute Of Technology Formation de nanostructure à base de carbone à l'aide de structures de croissance active à grande échelle
WO2014134484A1 (fr) 2013-02-28 2014-09-04 N12 Technologies, Inc. Distribution à base de cartouche de film de nanostructure
JP6039534B2 (ja) 2013-11-13 2016-12-07 東京エレクトロン株式会社 カーボンナノチューブの生成方法及び配線形成方法

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5037785A (en) * 1989-11-17 1991-08-06 Her Majesty The Queen In Right Of Canada, As Represented By The Minister Of Energy, Mines And Resources Catalyst regeneration process using laser radiation
US20020088938A1 (en) * 1996-08-08 2002-07-11 William Marsh Rice University Method for forming an array of single-wall carbon nanotubes and compositions thereof
US20020110513A1 (en) * 1998-09-18 2002-08-15 Margrave John L. Chemical derivatization of single-wall carbon nanotubes to facilitate solvation thereof; and use of derivatized nanotubes to form catalyst-containing seed materials for use in making carbon fibers
US20030042128A1 (en) * 2001-06-15 2003-03-06 Avetik Harutyunyan Method of purifying nanotubes and nanofibers using electromagnetic radiation
US20030124717A1 (en) * 2001-11-26 2003-07-03 Yuji Awano Method of manufacturing carbon cylindrical structures and biopolymer detection device
US6645455B2 (en) * 1998-09-18 2003-11-11 William Marsh Rice University Chemical derivatization of single-wall carbon nanotubes to facilitate solvation thereof; and use of derivatized nanotubes to form catalyst-containing seed materials for use in making carbon fibers
US20040101467A1 (en) * 2002-11-26 2004-05-27 Avetik Harutyunyan Method for synthesis of carbon nanotubes
US6869583B2 (en) * 2001-04-12 2005-03-22 The Penn State Research Foundation Purification of carbon filaments and their use in storing hydrogen
US20060057388A1 (en) * 2004-09-10 2006-03-16 Sungho Jin Aligned and open-ended nanotube structure and method for making the same
US20070009421A1 (en) * 2004-12-01 2007-01-11 William Marsh Rice University Fibers comprised of epitaxially grown single-wall carbon nanotubes, and a method for added catalyst and continuous growth at the tip

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3441923B2 (ja) * 1997-06-18 2003-09-02 キヤノン株式会社 カーボンナノチューブの製法
AUPP976499A0 (en) * 1999-04-16 1999-05-06 Commonwealth Scientific And Industrial Research Organisation Multilayer carbon nanotube films
WO2005033001A2 (fr) * 2003-09-03 2005-04-14 Honda Motor Co., Ltd. Procedes pour preparer des nanostructures de carbone unidimensionnelle
JP2005343744A (ja) * 2004-06-03 2005-12-15 Matsushita Electric Ind Co Ltd カーボンナノチューブ半導体の製造方法およびカーボンナノチューブ構造体
JP4868726B2 (ja) * 2004-09-14 2012-02-01 富士通株式会社 カーボンナノチューブの構造を制御する方法
JP4780546B2 (ja) * 2004-11-08 2011-09-28 学校法人 名城大学 カーボンナノチューブの作製方法及び電流制御素子の作製方法

Patent Citations (28)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5037785A (en) * 1989-11-17 1991-08-06 Her Majesty The Queen In Right Of Canada, As Represented By The Minister Of Energy, Mines And Resources Catalyst regeneration process using laser radiation
US6824755B2 (en) * 1996-08-08 2004-11-30 William Marsh Rice University Method for producing a catalyst support and compositions thereof
US7048903B2 (en) * 1996-08-08 2006-05-23 William Marsh Rice University Macroscopically manipulable nanoscale devices made from nanotube assemblies
US20020102201A1 (en) * 1996-08-08 2002-08-01 William Marsh Rice University Method for forming an array of single-wall carbon nanotubes in an electric field and compositions thereof
US7052666B2 (en) * 1996-08-08 2006-05-30 William Marsh Rice University Method for cutting single-wall carbon nanotubes
US20030010910A1 (en) * 1996-08-08 2003-01-16 William Marsh Rice University Continuous fiber of single-wall carbon nanotubes
US20020088938A1 (en) * 1996-08-08 2002-07-11 William Marsh Rice University Method for forming an array of single-wall carbon nanotubes and compositions thereof
US20030066960A1 (en) * 1996-08-08 2003-04-10 William Marsh Rice University Apparatus for growing continuous single-wall carbon nanotube fiber
US20030106998A1 (en) * 1996-08-08 2003-06-12 William Marsh Rice University Method for producing boron nitride coatings and fibers and compositions thereof
US20050244326A1 (en) * 1996-08-08 2005-11-03 William Marsh Rice University Method for fractionating single-wall carbon nanotubes
US6939525B2 (en) * 1996-08-08 2005-09-06 William Marsh Rice University Method of forming composite arrays of single-wall carbon nanotubes and compositions thereof
US20040265209A1 (en) * 1996-08-08 2004-12-30 William Marsh Rice University Method for end-derivatizing single-wall carbon nanotubes and for introducing an endohedral group to single-wall carbon nanotubes
US6756026B2 (en) * 1996-08-08 2004-06-29 William Marsh Rice University Method for growing continuous carbon fiber and compositions thereof
US20020092984A1 (en) * 1996-08-08 2002-07-18 William Marsh Rice University Method for purification of as-produced single-wall carbon nanotubes
US6756025B2 (en) * 1996-08-08 2004-06-29 William Marsh Rice University Method for growing single-wall carbon nanotubes utilizing seed molecules
US20020110513A1 (en) * 1998-09-18 2002-08-15 Margrave John L. Chemical derivatization of single-wall carbon nanotubes to facilitate solvation thereof; and use of derivatized nanotubes to form catalyst-containing seed materials for use in making carbon fibers
US6835366B1 (en) * 1998-09-18 2004-12-28 William Marsh Rice University Chemical derivatization of single-wall carbon nanotubes to facilitate solvation thereof, and use of derivatized nanotubes
US6841139B2 (en) * 1998-09-18 2005-01-11 William Marsh Rice University Methods of chemically derivatizing single-wall carbon nanotubes
US6875412B2 (en) * 1998-09-18 2005-04-05 William Marsh Rice University Chemically modifying single wall carbon nanotubes to facilitate dispersal in solvents
US6827918B2 (en) * 1998-09-18 2004-12-07 William Marsh Rice University Dispersions and solutions of fluorinated single-wall carbon nanotubes
US6645455B2 (en) * 1998-09-18 2003-11-11 William Marsh Rice University Chemical derivatization of single-wall carbon nanotubes to facilitate solvation thereof; and use of derivatized nanotubes to form catalyst-containing seed materials for use in making carbon fibers
US6869583B2 (en) * 2001-04-12 2005-03-22 The Penn State Research Foundation Purification of carbon filaments and their use in storing hydrogen
US7014737B2 (en) * 2001-06-15 2006-03-21 Penn State Research Foundation Method of purifying nanotubes and nanofibers using electromagnetic radiation
US20030042128A1 (en) * 2001-06-15 2003-03-06 Avetik Harutyunyan Method of purifying nanotubes and nanofibers using electromagnetic radiation
US20030124717A1 (en) * 2001-11-26 2003-07-03 Yuji Awano Method of manufacturing carbon cylindrical structures and biopolymer detection device
US20040101467A1 (en) * 2002-11-26 2004-05-27 Avetik Harutyunyan Method for synthesis of carbon nanotubes
US20060057388A1 (en) * 2004-09-10 2006-03-16 Sungho Jin Aligned and open-ended nanotube structure and method for making the same
US20070009421A1 (en) * 2004-12-01 2007-01-11 William Marsh Rice University Fibers comprised of epitaxially grown single-wall carbon nanotubes, and a method for added catalyst and continuous growth at the tip

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20100081568A1 (en) * 2008-04-21 2010-04-01 Lockheed Martin Corporation Methods for producing carbon nanotubes with controlled chirality and diameter and products therefrom
US20090274609A1 (en) * 2008-05-01 2009-11-05 Honda Motor Co., Ltd. Synthesis Of High Quality Carbon Single-Walled Nanotubes
US20090324484A1 (en) * 2008-05-01 2009-12-31 Honda Motor Co., Ltd. Effect Of Hydrocarbon And Transport Gas Feedstock On Efficiency And Quality Of Grown Single-Walled Nanotubes
US8591858B2 (en) 2008-05-01 2013-11-26 Honda Motor Co., Ltd. Effect of hydrocarbon and transport gas feedstock on efficiency and quality of grown single-walled nanotubes
US9174847B2 (en) * 2008-05-01 2015-11-03 Honda Motor Co., Ltd. Synthesis of high quality carbon single-walled nanotubes
US10850984B2 (en) 2008-05-01 2020-12-01 Honda Motor Co., Ltd. Synthesis of high quality carbon single-walled nanotubes
CN117623287A (zh) * 2023-11-16 2024-03-01 江西铜业技术研究院有限公司 一种高导电碳包覆单壁碳纳米管碳网及制备方法和应用

Also Published As

Publication number Publication date
JP5358045B2 (ja) 2013-12-04
JP2010503595A (ja) 2010-02-04
WO2008100325A2 (fr) 2008-08-21
WO2008100325A3 (fr) 2008-10-30

Similar Documents

Publication Publication Date Title
JP5358045B2 (ja) カーボンナノチューブの製造方法
CN1248959C (zh) 一种碳纳米管阵列生长方法
Hong et al. Controlling the growth of single-walled carbon nanotubes on surfaces using metal and non-metal catalysts
US7235159B2 (en) Methods for producing and using catalytic substrates for carbon nanotube growth
CN101039873B (zh) 碳纳米管集合体及其制造方法
JPWO2004071654A1 (ja) 単層カーボンナノチューブ製造用触媒金属微粒子形成方法
WO2009145959A1 (fr) Système de culture de nanotube de carbone à haut débit, et nanotubes de carbone et nanofibres de carbone ainsi formées
JP2011519808A (ja) 高品質なカーボン単層ナノチューブの合成
WO2010014650A2 (fr) Croissance préférentielle de nanotubes de carbone à paroi unique avec une conductivité métallique
KR20160057393A (ko) 탄소 나노구조체의 제조 방법 및 카본 나노튜브
JPWO2006025393A1 (ja) ナノスケールの低次元量子構造体の製造方法、及び、当該製造方法を用いた集積回路の製造方法
US20050214197A1 (en) Methods for producing and using catalytic substrates for carbon nanotube growth
JP4834957B2 (ja) 触媒構造体およびこれを用いたカーボンナノチューブの製造方法
JP5770166B2 (ja) 調整可能な新種のガス貯蔵材料及びガス感知材料
JP6202359B2 (ja) カーボンナノチューブの製造方法
Rohmund et al. Carbon nanotube films grown by laser-assisted chemical vapor deposition
US20080279752A1 (en) Method for producing a single-wall carbon nanotube
JP2007268319A (ja) カーボンナノチューブ合成用触媒及びその製造方法、触媒分散液、並びに、カーボンナノチューブの製造方法
JP2010077007A (ja) カーボンナノチューブ形成用基材及び該基材に配向成長したカーボンナノチューブ並びにこれらの製造方法
Ryu et al. Synthesis and Optimization of MWCNTs on Co‐Ni/MgO by Thermal CVD
JP2012140268A (ja) カーボンナノチューブ生成用基材の判定方法およびカーボンナノチューブの製造方法
JP2016088815A (ja) 炭素ナノ構造体集合物およびその製造方法
TWI246503B (en) Method for producing a carbon nanotube array
JP6171805B2 (ja) 炭素ナノ構造体の製造方法
Kang et al. Nanopatterning of catalyst by Dip Pen nanolithography (DPN) for synthesis of carbon nanotubes (CNT)

Legal Events

Date Code Title Description
AS Assignment

Owner name: HONDA MOTOR CO., LTD., JAPAN

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:HARUTYUNYAN, AVETIK;REEL/FRAME:018240/0963

Effective date: 20060901

STCB Information on status: application discontinuation

Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION