CN1696052A - A method for preparing carbon nanotubes - Google Patents
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- CN1696052A CN1696052A CN 200410018203 CN200410018203A CN1696052A CN 1696052 A CN1696052 A CN 1696052A CN 200410018203 CN200410018203 CN 200410018203 CN 200410018203 A CN200410018203 A CN 200410018203A CN 1696052 A CN1696052 A CN 1696052A
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 49
- 239000002041 carbon nanotube Substances 0.000 title claims abstract description 44
- 229910021393 carbon nanotube Inorganic materials 0.000 title claims abstract description 43
- 238000000034 method Methods 0.000 title claims abstract description 13
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 14
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 claims abstract description 11
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 claims abstract description 11
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims abstract description 10
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 8
- QQONPFPTGQHPMA-UHFFFAOYSA-N Propene Chemical compound CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 claims abstract description 6
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- 239000000377 silicon dioxide Substances 0.000 claims abstract description 4
- 235000012239 silicon dioxide Nutrition 0.000 claims abstract 3
- 239000003054 catalyst Substances 0.000 claims description 24
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 10
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 10
- 239000001257 hydrogen Substances 0.000 claims description 9
- 229910052739 hydrogen Inorganic materials 0.000 claims description 9
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 8
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 7
- 239000007789 gas Substances 0.000 claims description 7
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 6
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical compound CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 claims description 6
- 239000002048 multi walled nanotube Substances 0.000 claims description 6
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims description 5
- 239000002253 acid Substances 0.000 claims description 5
- 229910021529 ammonia Inorganic materials 0.000 claims description 5
- 238000005336 cracking Methods 0.000 claims description 5
- 229930195733 hydrocarbon Natural products 0.000 claims description 5
- 150000002430 hydrocarbons Chemical class 0.000 claims description 5
- 229910052757 nitrogen Inorganic materials 0.000 claims description 5
- 239000002245 particle Substances 0.000 claims description 5
- 229910002651 NO3 Inorganic materials 0.000 claims description 4
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 claims description 4
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 claims description 4
- 239000012299 nitrogen atmosphere Substances 0.000 claims description 4
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 claims description 4
- LFQCEHFDDXELDD-UHFFFAOYSA-N tetramethyl orthosilicate Chemical group CO[Si](OC)(OC)OC LFQCEHFDDXELDD-UHFFFAOYSA-N 0.000 claims description 4
- 239000005909 Kieselgur Substances 0.000 claims description 3
- 239000003513 alkali Substances 0.000 claims description 3
- 239000000956 alloy Substances 0.000 claims description 3
- 229910045601 alloy Inorganic materials 0.000 claims description 3
- 229910052786 argon Inorganic materials 0.000 claims description 3
- 230000015572 biosynthetic process Effects 0.000 claims description 3
- -1 carbon ions Chemical class 0.000 claims description 3
- 239000000969 carrier Substances 0.000 claims description 3
- 239000004927 clay Substances 0.000 claims description 3
- UFMZWBIQTDUYBN-UHFFFAOYSA-N cobalt dinitrate Chemical compound [Co+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O UFMZWBIQTDUYBN-UHFFFAOYSA-N 0.000 claims description 3
- 229910001981 cobalt nitrate Inorganic materials 0.000 claims description 3
- 239000003085 diluting agent Substances 0.000 claims description 3
- 239000001307 helium Substances 0.000 claims description 3
- 229910052734 helium Inorganic materials 0.000 claims description 3
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 claims description 3
- 150000002431 hydrogen Chemical class 0.000 claims description 3
- 239000000395 magnesium oxide Substances 0.000 claims description 3
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Substances [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 3
- 229910052759 nickel Inorganic materials 0.000 claims description 3
- 239000010453 quartz Substances 0.000 claims description 3
- 239000002109 single walled nanotube Substances 0.000 claims description 3
- 239000011240 wet gel Substances 0.000 claims description 3
- DDFHBQSCUXNBSA-UHFFFAOYSA-N 5-(5-carboxythiophen-2-yl)thiophene-2-carboxylic acid Chemical compound S1C(C(=O)O)=CC=C1C1=CC=C(C(O)=O)S1 DDFHBQSCUXNBSA-UHFFFAOYSA-N 0.000 claims description 2
- 239000003377 acid catalyst Substances 0.000 claims description 2
- 239000007864 aqueous solution Substances 0.000 claims description 2
- 239000002585 base Substances 0.000 claims description 2
- 239000007853 buffer solution Substances 0.000 claims description 2
- 239000000499 gel Substances 0.000 claims description 2
- 238000010438 heat treatment Methods 0.000 claims description 2
- 238000006460 hydrolysis reaction Methods 0.000 claims description 2
- KBJMLQFLOWQJNF-UHFFFAOYSA-N nickel(ii) nitrate Chemical compound [Ni+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O KBJMLQFLOWQJNF-UHFFFAOYSA-N 0.000 claims description 2
- 238000003980 solgel method Methods 0.000 claims description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims 1
- MVFCKEFYUDZOCX-UHFFFAOYSA-N iron(2+);dinitrate Chemical group [Fe+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O MVFCKEFYUDZOCX-UHFFFAOYSA-N 0.000 claims 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 claims 1
- 238000005229 chemical vapour deposition Methods 0.000 abstract description 3
- 229910052681 coesite Inorganic materials 0.000 abstract 1
- 229910052906 cristobalite Inorganic materials 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 239000003863 metallic catalyst Substances 0.000 abstract 1
- 229910052682 stishovite Inorganic materials 0.000 abstract 1
- 229910052905 tridymite Inorganic materials 0.000 abstract 1
- 238000002360 preparation method Methods 0.000 description 8
- VCJMYUPGQJHHFU-UHFFFAOYSA-N iron(3+);trinitrate Chemical group [Fe+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O VCJMYUPGQJHHFU-UHFFFAOYSA-N 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 5
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- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical group [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 2
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 238000003917 TEM image Methods 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 235000011114 ammonium hydroxide Nutrition 0.000 description 2
- 238000003421 catalytic decomposition reaction Methods 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000011232 storage material Substances 0.000 description 2
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- 229910003481 amorphous carbon Inorganic materials 0.000 description 1
- 238000001241 arc-discharge method Methods 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
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- 238000000608 laser ablation Methods 0.000 description 1
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 1
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Abstract
Description
技术领域Technical field
本发明属于无机功能材料合成领域,更具体地说涉及催化剂的制备方法以及在高温下以碳源气体为原料(甲烷、乙烯或丙烯等)裂解制备碳纳米管的方法。The invention belongs to the field of synthesis of inorganic functional materials, and more specifically relates to a catalyst preparation method and a method for preparing carbon nanotubes by cracking carbon source gas (methane, ethylene or propylene, etc.) at high temperature as raw materials.
背景技术 Background technique
自1991年日本科学家Iijiam发现碳纳米管(CNTs)以来,由于其具有奇特的物理、化学性质和很好的应用前景而引起了各国科技人员的极大关注。科学家们预测,碳纳米管将成为21世纪最有前途的一维纳米材料。碳纳米管是以碳原子形成的六角形晶格为基础的圆柱形结构,具有单层结构的称为单壁碳纳米管(SWNT),具有多层结构的称为多壁碳纳米管(MWNTs)。理论预测和实验研究发现碳纳米管有非常奇特电学性质,与其结构密切相关,可用于制作晶体管等纳米电子器件。碳纳米管是一种很好的导热材料,依靠超声波传递热能。碳纳米管具有很高的强度和韧性,碳纳米管的杨氏弹性模量最高可达3.7Tpa,碳纳米管的密度仅为钢的1/7,但其抗拉强度却是钢的100倍。碳纳米管具有很大的比表面积,是理想的储氢材料。另外,碳纳米管耐酸碱、耐高温,但可以衍生物化,又因具有很好的机械强度和优异的导电性,因此可用来制备复合材料、化学传感材料和人工肌肉。Since the Japanese scientist Iijiam discovered carbon nanotubes (CNTs) in 1991, they have attracted great attention from scientists and technicians from various countries because of their unique physical and chemical properties and good application prospects. Scientists predict that carbon nanotubes will become the most promising one-dimensional nanomaterials in the 21st century. Carbon nanotubes are cylindrical structures based on hexagonal lattices formed by carbon atoms. Those with a single-layer structure are called single-walled carbon nanotubes (SWNTs), and those with a multi-layered structure are called multi-walled carbon nanotubes (MWNTs). ). Theoretical predictions and experimental studies have found that carbon nanotubes have very peculiar electrical properties, which are closely related to their structures, and can be used to make nanoelectronic devices such as transistors. Carbon nanotubes are a good heat-conducting material, relying on ultrasonic waves to transmit heat energy. Carbon nanotubes have high strength and toughness. The Young's modulus of carbon nanotubes can reach up to 3.7Tpa. The density of carbon nanotubes is only 1/7 of that of steel, but its tensile strength is 100 times that of steel. . Carbon nanotubes have a large specific surface area and are ideal hydrogen storage materials. In addition, carbon nanotubes are resistant to acid, alkali and high temperature, but can be derivatized, and because of their good mechanical strength and excellent electrical conductivity, they can be used to prepare composite materials, chemical sensing materials and artificial muscles.
碳纳米管自被发现以来,其制备工艺得到了广泛研究。现已有多种制备方法,如电弧放电法、激光烧蚀、电解、低温固体裂解、碳氢化合物催化分解或化学气相沉积法等。其中,化学气相沉积法是目前较为广泛的一种制备碳纳米管的方法。一般选用Fe、Co、Ni及其合金作为催化剂,粘土、二氧化硅、硅藻土、氧化铝及氧化镁等作为载体,乙炔、丙烯及甲烷等作为碳源,氢气、氮气、氦气、氩气或氨气作为稀释气,在530℃~1130℃范围内,碳氢化合物裂解产生的自由碳离子在催化剂作用下可生成单壁或多壁碳纳米管。其所需的设备和工艺条件都相对简单,适用于碳纳米管的大规模制备。但是其大小不均,长短不一,有缺陷,其关键是催化的制备和分散。目前制备无序、非定向的多壁碳纳米管粗产品中含有大量的无定形炭、纳米炭颗粒及催化剂粒子等杂质,存在较多的结晶缺陷,不易分散,常常发生弯曲和变形,石墨化程度较差,这些缺点对碳纳米管的力学性能及物化性能会有不良的影响。在碳纳米管的制备工艺中,催化剂的组成、原料气的种类、反应温度等都不同程度地影响碳纳米管的产量、质量以及微观结构。因此,开发一种碳纳米管产量高、质量好、使用效果好的制备方法已成为烃类催化分解法研制中需要解决的关键技术之一。Since the discovery of carbon nanotubes, their preparation process has been extensively studied. There are many preparation methods, such as arc discharge method, laser ablation, electrolysis, low-temperature solid cracking, catalytic decomposition of hydrocarbons or chemical vapor deposition. Among them, the chemical vapor deposition method is currently a widely used method for preparing carbon nanotubes. Generally, Fe, Co, Ni and their alloys are used as catalysts, clay, silica, diatomaceous earth, alumina and magnesia are used as carriers, acetylene, propylene and methane are used as carbon sources, hydrogen, nitrogen, helium, argon Gas or ammonia as diluent gas, in the range of 530°C to 1130°C, the free carbon ions produced by the cracking of hydrocarbons can generate single-wall or multi-wall carbon nanotubes under the action of the catalyst. The required equipment and process conditions are relatively simple, and are suitable for large-scale preparation of carbon nanotubes. However, its size is uneven, its length is different, and it has defects. The key is the preparation and dispersion of catalysis. At present, the rough products of disordered and non-oriented multi-walled carbon nanotubes contain a large amount of impurities such as amorphous carbon, nano-carbon particles and catalyst particles, and there are many crystal defects, which are not easy to disperse, often bend and deform, and graphitize. To a lesser extent, these shortcomings will have a negative impact on the mechanical properties and physical and chemical properties of carbon nanotubes. In the preparation process of carbon nanotubes, the composition of the catalyst, the type of raw gas, and the reaction temperature all affect the yield, quality and microstructure of carbon nanotubes to varying degrees. Therefore, the development of a carbon nanotube preparation method with high yield, good quality and good use effect has become one of the key technologies to be solved in the development of catalytic decomposition of hydrocarbons.
发明内容Contents of Invention
本发明的目的在于提出一种成本低廉、简单易行,碳纳米管的质量好,产量高的制备方法。The object of the present invention is to provide a low-cost, simple and easy preparation method with good quality and high yield of carbon nanotubes.
技术方案如下:The technical solution is as follows:
选用Fe、Co、Ni及其合金作为催化剂,粘土、二氧化硅、硅藻土、氧化铝及氧化镁等作为载体,乙炔、丙烯及甲烷等作为碳源,氢气、氮气、氦气、氩气或氨气作为稀释气,在530℃~1130℃范围内,碳氢化合物裂解产生的自由碳离子在催化剂作用下可生成单壁或多壁碳纳米管;Fe, Co, Ni and their alloys are selected as catalysts, clay, silica, diatomaceous earth, alumina and magnesium oxide are used as carriers, acetylene, propylene and methane are used as carbon sources, hydrogen, nitrogen, helium, argon Or ammonia as a diluent gas, in the range of 530 ° C ~ 1130 ° C, the free carbon ions produced by the cracking of hydrocarbons can generate single-walled or multi-walled carbon nanotubes under the action of a catalyst;
(1)以溶胶-凝胶法制备催化剂:硅酸酯(AR),乙醇((AR)和(0.5-2M)硝酸盐(AR)水溶液以1∶1∶1(体积比)混合,充分搅拌均匀,然后加入几滴酸或碱作催化剂来加快水解反应,促进凝胶的形成;把湿凝胶在40~60℃的恒温下干燥,得到干凝胶;然后把干凝胶研磨成颗粒作为催化剂;(1) Prepare catalyst by sol-gel method: Silicate (AR), ethanol ((AR) and (0.5-2M) nitrate (AR) aqueous solution are mixed with 1: 1: 1 (volume ratio), fully stirred Evenly, then add a few drops of acid or alkali as a catalyst to speed up the hydrolysis reaction and promote the formation of the gel; dry the wet gel at a constant temperature of 40-60°C to obtain a xerogel; then grind the xerogel into particles as catalyst;
(2)把所制得的粉末状催化剂平铺于石英舟上,放入管式加热炉中的恒温区,在氮气保护下,升温至400~800℃,通入氢气20~40分钟,还原催化剂,然后加热到600~1000℃,通入乙炔,反应30~120分钟,在氮气的气氛下冷却到常温,即制备出了碳纳米管。(2) Spread the prepared powdered catalyst on a quartz boat, put it into the constant temperature zone of the tubular heating furnace, raise the temperature to 400-800°C under the protection of nitrogen, and pass in hydrogen for 20-40 minutes to reduce The catalyst is then heated to 600-1000° C., passed through acetylene, reacted for 30-120 minutes, cooled to normal temperature under nitrogen atmosphere, and the carbon nanotubes are prepared.
所述的硅酸酯是正硅酸甲酯Si(OCH3)4(TMOS)或正硅酸乙酯Si(OC2H5)4(TEOS)。The silicate is methyl orthosilicate Si(OCH 3 ) 4 (TMOS) or ethyl orthosilicate Si(OC 2 H 5 ) 4 (TEOS).
所述的硝酸盐为硝酸铁,硝酸钴和硝酸镍。Described nitrate is ferric nitrate, cobalt nitrate and nickel nitrate.
所述的酸催化剂为质子酸,碱催化剂为氨水或氨水与氟化铵的缓冲溶液。The acid catalyst is a protonic acid, and the base catalyst is ammonia water or a buffer solution of ammonia water and ammonium fluoride.
利用本发明的实验方法制备碳纳米管的过程简单,易操作,成本较低,产率大;制得了大量管径均匀的碳纳米管,内径5~20nm,外径在20~50nm。The process of preparing carbon nanotubes by using the experimental method of the invention is simple, easy to operate, low in cost and high in yield; a large number of carbon nanotubes with uniform diameters are produced, with an inner diameter of 5-20nm and an outer diameter of 20-50nm.
采用本法制备的碳纳米管产物中的杂质含量少,石墨化程度高,碳纳米管的管径比较均匀,表面比较光滑,经纯化后的碳纳米管可直接用来研制复合材料或用作气体储存材料。The impurity content in the carbon nanotube product prepared by this method is small, the degree of graphitization is high, the tube diameter of the carbon nanotube is relatively uniform, and the surface is relatively smooth, and the purified carbon nanotube can be directly used to develop composite materials or used as Gas storage materials.
附图说明Description of drawings
图1是实施一采用本发明制备的碳纳米管的透射电镜照片;Fig. 1 is to implement a transmission electron microscope photograph adopting the carbon nanotube prepared by the present invention;
图2是实施一采用本发明制备的碳纳米管的扫描电镜照片;Fig. 2 is a scanning electron micrograph of implementing a carbon nanotube prepared by the present invention;
图3是实施四采用本发明制备的碳纳米管的透射电镜照片;Fig. 3 is the transmission electron micrograph of the carbon nanotube prepared by the present invention;
图4是实施四采用本发明制备的碳纳米管的局部透射电镜照片。Fig. 4 is a partial transmission electron micrograph of carbon nanotubes prepared by the present invention in Embodiment 4.
具体实施方式 Detailed ways
本发明内容通过以下的实施例和附图作进一步阐述,但并不限制本发明的范围。The content of the present invention is further illustrated by the following examples and accompanying drawings, but does not limit the scope of the present invention.
实施例一Embodiment one
2M硝酸铁10ml(AR)与正硅酸乙酯(AR)10ml及乙醇(AR)10ml混合,充分搅拌约30分钟。然后缓慢加入约0.3ml的氢氟酸(AR),进一步搅拌均匀。制出湿凝胶,把湿凝胶在恒温60℃下干燥7天,研磨成均匀颗粒作为催化剂。把粉末状催化剂100mg平铺在石英舟上,放于管式炉的恒温区中,在氮气气氛下(流量为500ml/min)升温到400℃,通入氢气,流量为300ml/min,还原25min,升温至600℃,通入乙炔,流量为50ml/min,反应60min,在氮气的气氛下冷却。即制备出了碳纳米管,得到的产品产量为133mg。Mix 10ml of 2M ferric nitrate (AR), 10ml of ethyl orthosilicate (AR) and 10ml of ethanol (AR), and stir thoroughly for about 30 minutes. Then slowly add about 0.3ml of hydrofluoric acid (AR), and further stir evenly. The wet gel was prepared, dried at a constant temperature of 60° C. for 7 days, and ground into uniform particles as a catalyst. Spread 100mg of powdered catalyst on a quartz boat, put it in the constant temperature zone of the tube furnace, raise the temperature to 400°C under nitrogen atmosphere (flow rate: 500ml/min), feed hydrogen gas, flow rate: 300ml/min, and reduce for 25min , the temperature was raised to 600° C., acetylene was passed through at a flow rate of 50 ml/min, the reaction was carried out for 60 min, and the mixture was cooled under nitrogen atmosphere. That is, carbon nanotubes were prepared, and the yield of the obtained product was 133 mg.
实施例二Embodiment two
与实施例一其他条件和步骤相同,改变乙炔的反应温度为800℃,得到碳纳米管的产量为156mg。The other conditions and steps were the same as in Example 1, but the reaction temperature of acetylene was changed to 800° C., and the yield of carbon nanotubes was 156 mg.
实施例三Embodiment Three
与实施例一其他条件和步骤相同,改变乙炔的反应温度为1000℃,得到的碳纳米管的产量为189mg。The other conditions and steps were the same as in Example 1, but the reaction temperature of acetylene was changed to 1000° C., and the yield of carbon nanotubes obtained was 189 mg.
实施例四Embodiment Four
与实施例一其他条件和步骤相同,改变氢气反应温度为750℃,乙炔通入的时间为30min。得到的碳纳米管的产量为76.6mg。The other conditions and steps are the same as in Example 1, changing the hydrogen reaction temperature to 750° C., and the acetylene feeding time to 30 minutes. The yield of the obtained carbon nanotubes was 76.6 mg.
实施例五Embodiment five
与实施例一其他条件和步骤相同,改变氢气的流量为100ml/min。得到的碳纳米管的产量为162mg。The other conditions and steps are the same as in Example 1, changing the flow rate of hydrogen to 100ml/min. The yield of carbon nanotubes obtained was 162 mg.
实施例六Embodiment six
与实施例一其他条件和步骤相同,改变氢气的流量为100ml/min,乙炔通入的温度为800℃。得到的碳纳米管的产量为171.1mg。The other conditions and steps are the same as in Example 1, changing the flow rate of hydrogen to 100ml/min, and the temperature of acetylene to 800°C. The yield of the obtained carbon nanotubes was 171.1 mg.
实施例七Embodiment seven
与实施例一其他条件和步骤相同,采用0.5M硝酸铁10ml(AR)与正硅酸乙酯(AR)10ml乙醇(AR)10ml混合。得到碳纳米管的产量为156mg。Other conditions and steps are the same as in Example 1, 10ml of 0.5M ferric nitrate (AR) is mixed with 10ml of ethyl orthosilicate (AR) and 10ml of ethanol (AR). The yield of carbon nanotubes obtained was 156 mg.
实施例八Embodiment Eight
与实施例一其他条件和步骤相同,采用0.5M硝酸钴10ml(AR)来制备催化剂,得到的碳纳米管的产量为178.5mg。Other conditions and steps were the same as in Example 1, 10 ml of 0.5M cobalt nitrate (AR) was used to prepare the catalyst, and the yield of the obtained carbon nanotubes was 178.5 mg.
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