KR20020025101A - mass production of carbon nanotubes by pyrolysis - Google Patents
mass production of carbon nanotubes by pyrolysis Download PDFInfo
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- KR20020025101A KR20020025101A KR1020020001392A KR20020001392A KR20020025101A KR 20020025101 A KR20020025101 A KR 20020025101A KR 1020020001392 A KR1020020001392 A KR 1020020001392A KR 20020001392 A KR20020001392 A KR 20020001392A KR 20020025101 A KR20020025101 A KR 20020025101A
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title abstract description 19
- 239000002041 carbon nanotube Substances 0.000 title abstract description 19
- 229910021393 carbon nanotube Inorganic materials 0.000 title abstract description 19
- 238000004519 manufacturing process Methods 0.000 title abstract description 4
- 238000000197 pyrolysis Methods 0.000 title description 2
- 239000002071 nanotube Substances 0.000 claims abstract description 9
- 238000002347 injection Methods 0.000 claims description 5
- 239000007924 injection Substances 0.000 claims description 5
- 239000000463 material Substances 0.000 claims description 3
- 239000002826 coolant Substances 0.000 claims 1
- 229930195733 hydrocarbon Natural products 0.000 abstract description 12
- 150000002430 hydrocarbons Chemical class 0.000 abstract description 12
- 239000002243 precursor Substances 0.000 abstract description 10
- 239000007789 gas Substances 0.000 abstract description 8
- 239000007788 liquid Substances 0.000 abstract description 7
- 238000000034 method Methods 0.000 abstract description 6
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 abstract description 5
- 239000011593 sulfur Substances 0.000 abstract description 5
- 229910052717 sulfur Inorganic materials 0.000 abstract description 5
- 229910052723 transition metal Inorganic materials 0.000 abstract description 5
- 150000003624 transition metals Chemical class 0.000 abstract description 5
- 230000002194 synthesizing effect Effects 0.000 abstract description 4
- 239000007791 liquid phase Substances 0.000 abstract description 3
- 239000012071 phase Substances 0.000 abstract description 3
- 239000007792 gaseous phase Substances 0.000 abstract 1
- 239000002109 single walled nanotube Substances 0.000 abstract 1
- 239000004215 Carbon black (E152) Substances 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 4
- 238000003786 synthesis reaction Methods 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- YTPLMLYBLZKORZ-UHFFFAOYSA-N Thiophene Chemical compound C=1C=CSC=1 YTPLMLYBLZKORZ-UHFFFAOYSA-N 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 238000005229 chemical vapour deposition Methods 0.000 description 2
- -1 ethylene, Propylene, methane Chemical class 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 1
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 1
- HOWJQLVNDUGZBI-UHFFFAOYSA-N butane;propane Chemical compound CCC.CCCC HOWJQLVNDUGZBI-UHFFFAOYSA-N 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000012018 catalyst precursor Substances 0.000 description 1
- ILZSSCVGGYJLOG-UHFFFAOYSA-N cobaltocene Chemical compound [Co+2].C=1C=C[CH-]C=1.C=1C=C[CH-]C=1 ILZSSCVGGYJLOG-UHFFFAOYSA-N 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 1
- KTWOOEGAPBSYNW-UHFFFAOYSA-N ferrocene Chemical compound [Fe+2].C=1C=C[CH-]C=1.C=1C=C[CH-]C=1 KTWOOEGAPBSYNW-UHFFFAOYSA-N 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 239000003915 liquefied petroleum gas Substances 0.000 description 1
- 239000008204 material by function Substances 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 239000002356 single layer Substances 0.000 description 1
- 239000007790 solid phase Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000002207 thermal evaporation Methods 0.000 description 1
- 229930192474 thiophene Natural products 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/15—Nano-sized carbon materials
- C01B32/158—Carbon nanotubes
- C01B32/16—Preparation
- C01B32/162—Preparation characterised by catalysts
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00002—Chemical plants
- B01J2219/00027—Process aspects
- B01J2219/00033—Continuous processes
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2202/00—Structure or properties of carbon nanotubes
- C01B2202/02—Single-walled nanotubes
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2202/00—Structure or properties of carbon nanotubes
- C01B2202/06—Multi-walled nanotubes
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/15—Nano-sized carbon materials
- C01B32/158—Carbon nanotubes
- C01B32/159—Carbon nanotubes single-walled
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Nanotechnology (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Carbon And Carbon Compounds (AREA)
Abstract
본 발명은 액상 또는 기상의 탄화수소를 전이금속 전구체와 함께 고온의 수직 반응로 안으로 공급하여, 탄화수소를 분해시켜 기상상태에서 나노튜브를 합성하는 방법이다. 본 발명에 의한 방법은 연속적인 탄화수소 및 전이금속의 공급이 가능하기 때문에 탄소나노튜브의 대량생산이 가능하다. 그리고 액상 또는 기상의 황전구체를 첨가하는 양에 따라 다층 탄소나노튜브와 단층 탄소나노튜브를 만들 수 있다.The present invention is a method for synthesizing nanotubes in a gas phase by supplying liquid or gaseous hydrocarbons together with a transition metal precursor into a high temperature vertical reactor. The method according to the present invention enables the mass production of carbon nanotubes because of the continuous supply of hydrocarbons and transition metals. In addition, multilayer carbon nanotubes and single-walled carbon nanotubes can be made according to the amount of the sulfur precursor in liquid or gaseous phase.
Description
본 발명은 액상및 기상의 탄화 수소를 분해하여 탄소나노튜브 합성하는 방법에 관한 것이다. 탄소 나노튜브는 직경이 수㎚ 내지 수십㎚이고 길이가 수십㎛ 내지 수백㎛로 구조의 비등방성이 크며, 단층(single wall), 다층(multi wall) 또는 다발(rope) 형태의 다양한 구조의 형상을 가진다. 이러한 탄소 나노튜브는 감긴 형태에 따라 도체 또는 반도체의 성질을 띠며, 직경에 따라 에너지 갭(energy gap)이 달라지고 준 일차원적 구조를 가지고 있어 독특한 양자 효과를 나타낸다. 또한, 탄소 나노튜브는 역학적으로 견고하고(강철의 100배정도), 화학적 안정성이 뛰어나며 열전도도가 높고 속이 비어 있는 특성을 가진다. 이와 같이 탄소 나노튜브는 상기한 특성을 나타낼 수 있어, 미시 및 거시적인 측면에서 다양한 응용이 예상되는 새로운 기능성 재료로 각광받고 있다. 이러한 탄소 나노튜브를 전자파 차폐, 전기 화학적 저장 장치(예를 들어, 2차 전지, 연료 전지 또는 수퍼 커패시터 (supercapacitor))의 전극 극판, 전계 방출 디스플레이 (Field Emission Display), 전자 증폭기 또는 가스 센서(sensor) 등에 적용하고자하는 시도 또는 연구가 활발히 이루어지고 있다. 그런데, 이러한 탄소 나노튜브의 응용 기술이 실용화되기 위해서는 고순도의 탄소나노튜브를 대량으로 합성하여야 한다. 현재, 탄소나노튜브를 합성하는 방법으로, 레이져를 이용하는 방법과 열 및 화학 기상 증착법, 플라즈마 화학 기상 증착법 등이 있으나, 이들은 순도는 높으나 대량으로 만들어내지 못하고 있다. 그리고 기존의 열분해법은 주로 수평로를 이용하여, 연속적인 나노튜브의 생산이 어려웠다. 이런 점이 탄소나노튜브의 상업성을 제한하는 요인이다.The present invention relates to a method for synthesizing carbon nanotubes by decomposing liquid and gaseous hydrocarbons. Carbon nanotubes are several nanometers to several tens of nanometers in diameter and tens of micrometers to hundreds of micrometers in length, which are largely anisotropic in structure and have various shapes in the form of single walls, multi walls, or bundles. Have These carbon nanotubes have the properties of conductors or semiconductors depending on the shape of the wound and have a unique one-dimensional structure with different energy gaps and diameters. In addition, carbon nanotubes are mechanically strong (about 100 times as much as steel), have excellent chemical stability, have high thermal conductivity, and have hollow properties. As such, carbon nanotubes may exhibit the above characteristics, and thus are attracting attention as new functional materials that are expected to have various applications in the microscopic and macroscopic aspects. These carbon nanotubes can be used for electromagnetic shielding, electrode plates of electrochemical storage devices (e.g., secondary cells, fuel cells, or supercapacitors), field emission displays, electronic amplifiers, or gas sensors. Attempts or research to apply to such has been actively made. However, in order for the application technology of the carbon nanotubes to be practical, high-purity carbon nanotubes should be synthesized in large quantities. Currently, as a method of synthesizing carbon nanotubes, there are methods using a laser, thermal and chemical vapor deposition, plasma chemical vapor deposition, and the like, but these have high purity but are not produced in large quantities. In the conventional pyrolysis method, the production of continuous nanotubes using a horizontal furnace was difficult. This is the limiting factor for the commercialization of carbon nanotubes.
본 발명이 이루고자 하는 기술적 과제는, 고온의 수직로에 액상 또는 기상의 탄화수소와 증기화한 액상 또는 고상의 전이금속 전구체 공급하여, 탄소나노튜브를 연속적으로 생산하는데 있다. 또한 액상 또는 기상의 황전구체를 공급함으로써 고순도의 다층 및 단층 나노튜브를 합성하는데 있다.The technical problem to be achieved by the present invention is to continuously produce a carbon nanotube by supplying a liquid phase or gaseous hydrocarbon and a vaporized liquid phase or solid phase transition metal precursor to a high temperature vertical furnace. In addition, by supplying a liquid or gaseous sulfur precursor to the synthesis of high-purity multi-layer and single-layer nanotubes.
도 1은 본 발명에 의한 탄소나노튜브 합성 장비의 개념도.1 is a conceptual diagram of a carbon nanotube synthesis equipment according to the present invention.
상기의 기술적 과제를 달성하기 위한 본 발명의 일 관점은, 탄화수소를 전이금속 전구체와 함께 고온의 수직 반응로 안으로 공급하여, 탄화수소를 분해시켜 기상 상태에서 나노튜브를 합성법과 합성된 나노튜브가 가스 흐름 및 중력에 의해 자동으로 아래쪽으로 이동, 수거되는 방법이다. 이를 위해 액상 또는 기상의 탄화수소를 전이금속 전구체와 함께 고온의 수직 반응로 안으로 공급하기 위한 장치와,공급된 물질을 분해시켜 기상상태에서 나노튜브를 합성하기 위한 수직의 반응로, 합성된 나노튜브를 모으는 수거장치를 포함한다.One aspect of the present invention for achieving the above technical problem, by supplying a hydrocarbon with a transition metal precursor into a high-temperature vertical reactor, the hydrocarbon is decomposed to synthesize the nanotubes in the gas phase state and the synthesized nanotubes gas flow And automatically moved downward and collected by gravity. To this end, a device for supplying liquid or gaseous hydrocarbons together with a transition metal precursor into a high temperature vertical reactor, and a vertical reaction for decomposing the supplied material to synthesize nanotubes in a gaseous state. Includes a collecting device.
도 1은 본 발명에 의한 탄소나노튜브의 합성 장치의 일실시예가 도시되어 있다.Figure 1 shows an embodiment of a device for synthesizing carbon nanotubes according to the present invention.
본 발명에 의한 탄소나노튜 대량 합성 장치(200)는 반응관 (110), 가열 장치(120, 121), 액체 및 기체의 탄화수소 공급장치(130), 황 전구체 및 촉매 금속 전구체 공급장치(140), 나노튜브 수거장치(150), 냉각할 수 있는 주입구(160)로 구성된다. 반응관(110)은 수직으로 놓여져 있으며, 위쪽에 주입구(160)가 놓이며, 분해된 가스 상태의 물질의 위쪽으로의 역류를 막기 위해, buffer 가스를 주입구와 반응로 사이로 공급해준다. 그리고, 주입구는 탄화수소 공급장치(130), 황 및 촉매 전구체 공급장치(140)와 연결되어 있다.Carbon nanotube mass synthesis apparatus 200 according to the present invention is a reaction tube 110, heating devices (120, 121), hydrocarbon and supply device 130 of the liquid and gas, sulfur precursor and catalyst metal precursor supply device 140 , Nanotube collection device 150, the cooling inlet 160 is configured. The reaction tube 110 is vertically placed, and the injection hole 160 is placed on the upper side, and the buffer gas is supplied between the injection hole and the reactor to prevent the reverse flow of the decomposed gaseous material upward. In addition, the injection port is connected to the hydrocarbon supply device 130, the sulfur and the catalyst precursor supply device 140.
본 발명에 사용되는 액체의 탄화수소로는 자이렌(xylene), 벤젠(benzene), 사이클로헥산(cyclohexane), 하이드로퓨란(hydrofuran) 등이며, 기상의 탄화수소로는 아세틸렌(acetylene), 에틸렌(etylene), 프로필렌(propylene), 메탄(methane), 에탄(ethane), 프로판(propane) 부탄(buthane) 및 LPG 등이 있으며, 황 전구체로는 황화 수소(hydrogen sulfide) 가스와 액상의 치오펜(thiophene) 등이 있으며, 촉매 금속을 포함하는 전구체로는 페로신(ferrocene),코발트신(cobaltocene), 니켈로신(nickellocene), 아이언 펜타카르보닐(iron pentacarbonyl), 및 프탈라시안류(iron, nickel, cobat-phytallocian)등이 있다.Liquid hydrocarbons used in the present invention include xylene, benzene, cyclohexane, hydrofuran, and the like. As gas phase hydrocarbons, acetylene, ethylene, Propylene, methane, ethane, propane butane and LPG, and sulfur precursors include hydrogen sulfide gas and liquid thiophene. Precursors containing catalytic metals include ferrocene, cobaltocene, nickelellocene, iron pentacarbonyl, and phthalocyanates. phytallocian).
본 발명의 탄소나노튜브 합성장치는 탄화수소및 촉매금속의 연속적인 공급과 합성된 나노튜브의 연속적인 수거도 또한 가능하여 탄소 나노튜브의 대량생산에 효과적이다.The carbon nanotube synthesis apparatus of the present invention is also capable of continuous supply of hydrocarbons and catalytic metals and continuous collection of synthesized nanotubes, which is effective for mass production of carbon nanotubes.
Claims (4)
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| KR1020020001392A KR20020025101A (en) | 2002-01-10 | 2002-01-10 | mass production of carbon nanotubes by pyrolysis |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2003097521A1 (en) * | 2002-05-17 | 2003-11-27 | Nano Plasma Center Co., Ltd. | Inductively coupled plasma reactor for producing nano-powder |
| FR2841233A1 (en) * | 2002-06-24 | 2003-12-26 | Commissariat Energie Atomique | METHOD AND DEVICE FOR PYROLYSIS DEPOSITION OF CARBON NANOTUBES |
| WO2004007361A3 (en) * | 2002-07-16 | 2004-04-01 | Univ Cambridge Tech | Method of synthesis of carbon nanomaterials |
| EP1445236A1 (en) * | 2003-02-05 | 2004-08-11 | Université de Liège | Method and apparatus for producing carbon nanotubes |
| CN1300259C (en) * | 2005-04-20 | 2007-02-14 | 天津大学 | Method for preparing nonlinear optical material of linkage nano carbon tubes of polythiophene methylene |
| KR101981675B1 (en) * | 2017-12-11 | 2019-05-24 | 한국과학기술연구원 | Apparatus for manufacturing CNT and Method of manufacturing CNT using the same |
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