US20100239491A1 - Method of producing carbon nanotubes - Google Patents
Method of producing carbon nanotubes Download PDFInfo
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- 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
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- carbon
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 135
- 238000000034 method Methods 0.000 title claims abstract description 84
- 239000002041 carbon nanotube Substances 0.000 title description 8
- 229910021393 carbon nanotube Inorganic materials 0.000 title description 8
- 239000003054 catalyst Substances 0.000 claims abstract description 89
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 61
- 239000002109 single walled nanotube Substances 0.000 claims abstract description 47
- 238000004140 cleaning Methods 0.000 claims abstract description 34
- 239000000758 substrate Substances 0.000 claims abstract description 22
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 28
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 25
- 238000000576 coating method Methods 0.000 claims description 24
- 239000011248 coating agent Substances 0.000 claims description 22
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- 229910052742 iron Inorganic materials 0.000 claims description 12
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- 229910052751 metal Inorganic materials 0.000 claims description 11
- 239000002184 metal Substances 0.000 claims description 10
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 9
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 8
- 229910003481 amorphous carbon Inorganic materials 0.000 claims description 6
- 230000005670 electromagnetic radiation Effects 0.000 claims description 6
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- 230000002829 reductive effect Effects 0.000 claims description 6
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- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 claims description 5
- 229910052750 molybdenum Inorganic materials 0.000 claims description 5
- 239000011733 molybdenum Substances 0.000 claims description 5
- 229910052759 nickel Inorganic materials 0.000 claims description 5
- 238000000623 plasma-assisted chemical vapour deposition Methods 0.000 claims description 5
- 238000002230 thermal chemical vapour deposition Methods 0.000 claims description 5
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 4
- 239000005977 Ethylene Substances 0.000 claims description 4
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 claims description 4
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 claims description 4
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 4
- 239000001569 carbon dioxide Substances 0.000 claims description 4
- 229910017052 cobalt Inorganic materials 0.000 claims description 4
- 239000010941 cobalt Substances 0.000 claims description 4
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims description 4
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 claims description 4
- 229910052707 ruthenium Inorganic materials 0.000 claims description 4
- 239000002048 multi walled nanotube Substances 0.000 claims description 3
- 239000002079 double walled nanotube Substances 0.000 claims description 2
- FGUUSXIOTUKUDN-IBGZPJMESA-N C1(=CC=CC=C1)N1C2=C(NC([C@H](C1)NC=1OC(=NN=1)C1=CC=CC=C1)=O)C=CC=C2 Chemical compound C1(=CC=CC=C1)N1C2=C(NC([C@H](C1)NC=1OC(=NN=1)C1=CC=CC=C1)=O)C=CC=C2 FGUUSXIOTUKUDN-IBGZPJMESA-N 0.000 claims 2
- 239000002071 nanotube Substances 0.000 abstract description 26
- 230000008569 process Effects 0.000 abstract description 13
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 18
- 239000007789 gas Substances 0.000 description 16
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 12
- 229910052786 argon Inorganic materials 0.000 description 9
- 239000000203 mixture Substances 0.000 description 8
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 7
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 6
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- 230000015572 biosynthetic process Effects 0.000 description 6
- VCJMYUPGQJHHFU-UHFFFAOYSA-N iron(3+);trinitrate Chemical compound [Fe+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O VCJMYUPGQJHHFU-UHFFFAOYSA-N 0.000 description 6
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 5
- 238000005755 formation reaction Methods 0.000 description 5
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- 239000000725 suspension Substances 0.000 description 4
- 229910000608 Fe(NO3)3.9H2O Inorganic materials 0.000 description 3
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 3
- 238000004630 atomic force microscopy Methods 0.000 description 3
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- 239000001307 helium Substances 0.000 description 3
- 229910052734 helium Inorganic materials 0.000 description 3
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 3
- 229930195733 hydrocarbon Natural products 0.000 description 3
- 150000002430 hydrocarbons Chemical class 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 239000000463 material Substances 0.000 description 3
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- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 230000009467 reduction Effects 0.000 description 3
- 239000000377 silicon dioxide Substances 0.000 description 3
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- 238000001069 Raman spectroscopy Methods 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
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- 125000004432 carbon atom Chemical group C* 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
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- 229910002804 graphite Inorganic materials 0.000 description 2
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- 238000000608 laser ablation Methods 0.000 description 2
- 229910044991 metal oxide Inorganic materials 0.000 description 2
- 150000004706 metal oxides Chemical class 0.000 description 2
- 239000002923 metal particle Substances 0.000 description 2
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- 238000009832 plasma treatment Methods 0.000 description 2
- 238000006722 reduction reaction Methods 0.000 description 2
- 238000004574 scanning tunneling microscopy Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229910019614 (NH4)6 Mo7 O24.4H2 O Inorganic materials 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- APUPEJJSWDHEBO-UHFFFAOYSA-P ammonium molybdate Chemical compound [NH4+].[NH4+].[O-][Mo]([O-])(=O)=O APUPEJJSWDHEBO-UHFFFAOYSA-P 0.000 description 1
- 229940010552 ammonium molybdate Drugs 0.000 description 1
- 235000018660 ammonium molybdate Nutrition 0.000 description 1
- 239000011609 ammonium molybdate Substances 0.000 description 1
- 238000001241 arc-discharge method Methods 0.000 description 1
- FIXLYHHVMHXSCP-UHFFFAOYSA-H azane;dihydroxy(dioxo)molybdenum;trioxomolybdenum;tetrahydrate Chemical compound N.N.N.N.N.N.O.O.O.O.O=[Mo](=O)=O.O=[Mo](=O)=O.O=[Mo](=O)=O.O=[Mo](=O)=O.O[Mo](O)(=O)=O.O[Mo](O)(=O)=O.O[Mo](O)(=O)=O FIXLYHHVMHXSCP-UHFFFAOYSA-H 0.000 description 1
- 239000002800 charge carrier Substances 0.000 description 1
- 238000010367 cloning Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
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- 230000000694 effects Effects 0.000 description 1
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- -1 for example Chemical class 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000003032 molecular docking Methods 0.000 description 1
- 239000011943 nanocatalyst Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000000644 propagated effect Effects 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
Classifications
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- B01J23/74—Iron group metals
- B01J23/745—Iron
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- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts 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
- B01J23/84—Catalysts 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
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- B82—NANOTECHNOLOGY
- B82Y—SPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
- B82Y30/00—Nanotechnology for materials or surface science, e.g. nanocomposites
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- B82Y40/00—Manufacture or treatment of nanostructures
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- C01B32/00—Carbon; Compounds thereof
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- B01J23/16—Catalysts 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
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- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
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- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/0201—Impregnation
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- B01J37/02—Impregnation, coating or precipitation
- B01J37/0234—Impregnation and coating simultaneously
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- C—CHEMISTRY; METALLURGY
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- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
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- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
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- C—CHEMISTRY; METALLURGY
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- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/10—Particle morphology extending in one dimension, e.g. needle-like
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
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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.
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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 |
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| US20100239491A1 true US20100239491A1 (en) | 2010-09-23 |
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| 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)
| 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 |
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|---|---|---|---|---|
| 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 |
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| US20100081568A1 (en) * | 2008-04-21 | 2010-04-01 | Lockheed Martin Corporation | Methods for producing carbon nanotubes with controlled chirality and diameter and products therefrom |
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| 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 |
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