CN115608372A - Iron-cobalt-based catalyst, carbon nano tube and preparation process thereof - Google Patents

Iron-cobalt-based catalyst, carbon nano tube and preparation process thereof Download PDF

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CN115608372A
CN115608372A CN202211121091.5A CN202211121091A CN115608372A CN 115608372 A CN115608372 A CN 115608372A CN 202211121091 A CN202211121091 A CN 202211121091A CN 115608372 A CN115608372 A CN 115608372A
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cobalt
iron
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nitrate
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CN115608372B (en
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刘保生
翟鲲鹏
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Henan Guotan Nanotechnology Co ltd
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    • 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
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    • B01J23/8898Manganese, technetium or rhenium containing also molybdenum
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Abstract

The invention provides an iron-cobalt-based catalyst, a carbon nano tube and a preparation process thereof, wherein the iron-cobalt-based catalyst is prepared from the following raw materials in percentage by mass: 7-7.5wt% of ferric nitrate, aluminum nitrate: 10-15wt%, 4-8wt% of ammonia water, 0.1-0.5wt% of ammonium molybdate, 1-5wt% of ammonium carbonate, 0.5-0.9wt% of manganese acetate, 1.5-2wt% of cobalt nitrate and H 2 O62-75 wt%; the preparation process of the carbon nano tube comprises the following steps: adding the iron-cobalt-based catalyst into the first main reactor, introducing nitrogen and propylene, and performing expansion cracking on the propylene under the action of the iron-cobalt-based catalyst to obtain a carbon nano tube seed material; and blowing the carbon nano tube seed material into the second main reactor, and then introducing nitrogen and propylene for reaction to obtain a carbon nano tube finished product. The iron-cobalt-based catalyst of the invention is beneficial to improving the purity of the carbon nano tubeAnd the content of impurities such as iron, cobalt and the like is reduced.

Description

Iron-cobalt-based catalyst, carbon nano tube and preparation process thereof
Technical Field
The invention relates to the technical field of carbon nano tubes, in particular to an iron-cobalt-based catalyst, a carbon nano tube and a preparation process thereof.
Background
The carbon nano tube prepared by chemical vapor deposition is prepared by adding a catalyst into a furnace body, and then introducing a carbon source gas in the atmosphere of protective gas to grow the carbon nano tube, wherein the carbon nano tube prepared by the existing iron-cobalt based catalyst has the problems of low purity, high content of impurities such as iron, cobalt and the like.
Disclosure of Invention
The invention provides an iron-cobalt-based catalyst, a carbon nano tube and a preparation process thereof, which can improve the purity of the carbon nano tube and reduce the content of impurities such as iron, cobalt and the like.
The technical scheme of the invention is realized as follows: an iron-cobalt-based catalyst is prepared from the following raw materials in percentage by mass: 7-7.5wt% of ferric nitrate, aluminum nitrate: 10-15wt%, ammonia water 4-8wt%, ammonium molybdate 0.1-0.5wt%, ammonium carbonate 1-5wt%, manganese acetate 0.5-0.9wt%, cobalt nitrate 1.5-2wt%, and H 2 O62-75wt%。
Further, 7-7.5wt% of ferric nitrate, aluminum nitrate: 11-12wt%, ammonia water 5-6wt%, ammonium molybdate 0.2-0.3wt%, ammonium carbonate 3wt%, manganese acetate 0.7-0.8wt%, cobalt nitrate 1.5-2wt%, and H 2 O 70-72wt%。
Further, iron nitrate 7.28wt%, aluminum nitrate: 11.3wt%, ammonia water 5.61wt%, ammonium molybdate 0.26wt%, ammonium carbonate 3wt%, manganese acetate 0.71wt%, cobalt nitrate 1.64wt%, and H 2 O 70.2wt%。
A preparation process of carbon nanotubes comprises the following steps:
(1) Adding the iron-cobalt-based catalyst into a first main reactor, then introducing nitrogen and propylene, and carrying out expansion cracking on the propylene under the action of the iron-cobalt-based catalyst in a nitrogen environment to obtain a carbon nano tube seed material;
(2) And blowing the carbon nano tube seed material into the second main reactor through nitrogen, and then introducing nitrogen and propylene for reaction to obtain a carbon nano tube finished product.
The carbon nano tube is prepared by adopting the preparation process.
The invention has the beneficial effects that:
the carbon nano tube prepared by the iron-cobalt-based catalyst is beneficial to reducing the content of metal impurities such as iron, cobalt and the like, reducing the resistivity of carbon nano tube powder and improving the purity of the carbon nano tube.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to the drawings without creative efforts.
FIG. 1 is a TEM image of carbon nanotubes in example 5 of the present invention.
Detailed Description
The technical solutions in the embodiments of the present invention are clearly and completely described below, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all embodiments. All other embodiments, which can be obtained by a person skilled in the art without inventive effort based on the embodiments of the present invention, are within the scope of the present invention.
The invention adopts nitrogen with the purity of 99.999 percent as protective gas and propylene with the purity of 99.6 percent.
Example 1
An iron-cobalt-based catalyst is prepared from the following raw materials in percentage by mass: 7wt% of iron nitrate, aluminum nitrate: 15wt%, ammonia water 6wt%, ammonium molybdate 0.2wt%, ammonium carbonate 4wt%, manganese acetate 0.8wt%, cobalt nitrate 1.5wt%, and H 2 O 65.5wt%。
Example 2
An iron-cobalt-based catalyst is prepared from the following raw materials in percentage by mass: 7.5wt% of iron nitrate, aluminum nitrate: 10wt%, ammonia water 5wt%, ammonium molybdate 0.5wt%, ammonium carbonate 3wt%, manganese acetate 0.5wt%, cobalt nitrate 2wt%, and H 2 O 71.5wt%。
Example 3
An iron-cobalt-based catalyst is prepared from the following raw materials in percentage by mass: 7.28wt% of iron nitrate, aluminum nitrate: 11.3wt%, 5.61wt% of ammonia water, 0.26wt% of ammonium molybdate, 3wt% of ammonium carbonate, 0.71wt% of manganese acetate, 1.64wt% of cobalt nitrate and H 2 O 70.2wt%。
Example 4
An iron-cobalt-based catalyst is prepared from the following raw materials in percentage by mass: 7wt% of iron nitrate, aluminum nitrate: 12wt%, 8wt% of ammonia water, 0.3wt% of ammonium molybdate, 5wt% of ammonium carbonate, 0.9wt% of manganese acetate, 1.5wt% of cobalt nitrate and H 2 O 65.3wt%。
The method of preparing an iron-cobalt-based catalyst according to examples 1 to 4, wherein the iron-cobalt-based catalyst was obtained by stirring the above-mentioned raw materials uniformly, dehydrating, baking (550 °), pulverizing, and sieving.
Example 5
A preparation process of carbon nanotubes comprises the following steps:
(1) Firstly, blowing protective gas into a main reactor and a gas preheating furnace and starting to heat, wherein the protective gas is nitrogen with the purity of 99.999 percent; after the temperature of the main reactor is raised to 600 ℃, adding 3kg of the iron-cobalt-based catalyst prepared in the embodiment 3 into the main reactor, then introducing nitrogen and propylene, in a nitrogen environment, expanding and cracking the propylene under the action of the iron-cobalt-based catalyst to obtain a carbon nano tube seed material, cooling the carbon nano tube seed material, and then blowing the cooled carbon nano tube seed material into a transfer tank through nitrogen;
(2) And blowing the carbon nanotube seed material into the second main reactor through nitrogen, then introducing nitrogen and propylene for reaction, after the reaction is finished, blowing the carbon nanotube seed material into the cooling tank through nitrogen, cooling to 80 degrees, and blowing the carbon nanotube seed material into a finished product tank through nitrogen to obtain a carbon nanotube finished product.
In the steps (1) and (2), the introduction of the gas is divided into ten stages, the gas comprises high-temperature propylene, low-temperature propylene, high-temperature nitrogen and low-temperature nitrogen, and the introduction amount is shown in the following table 1:
TABLE 1 gas introduction in the individual stages
Figure BDA0003846633100000031
Figure BDA0003846633100000041
Comparative example 1
This example is substantially the same as example 5 except that: an iron-cobalt-based catalyst is prepared from the following raw materials in percentage by mass: 7.6wt% of ferric nitrate, aluminum nitrate: 11.3wt%, 5.61wt% of ammonia water, 0.26wt% of ammonium molybdate, 3wt% of ammonium carbonate, 0.71wt% of manganese acetate, 1.32wt% of cobalt nitrate and H 2 O 70.2wt%。
The finished carbon nanotubes prepared in example 5 were examined as shown in table 2 below:
table 2 examination results of carbon nanotube finished products of example 5 and comparative example 1
Figure BDA0003846633100000042
As can be seen from table 2 above, the carbon nanotube product prepared in example 5 of the present invention has lower iron and cobalt contents in metal impurities, lower powder resistivity, and higher purity.
The above description is only for the purpose of illustrating the preferred embodiments of the present invention and is not to be construed as limiting the invention, and any modifications, equivalents, improvements and the like that fall within the spirit and principle of the present invention are intended to be included therein.

Claims (5)

1. The iron-cobalt-based catalyst is characterized by being prepared from the following raw materials in percentage by mass: 7-7.5wt% of ferric nitrate, aluminum nitrate: 10-15wt%, ammonia water 4-8wt%, ammonium molybdate 0.1-0.5wt%, ammonium carbonate 1-5wt%, manganese acetate 0.5-0.9wt%, cobalt nitrate 1.5-2wt%, and H 2 O 62-75wt%。
2. The iron-cobalt based catalyst according to claim 1, wherein the weight percentage of iron nitrate is 7-7.5%, and the weight percentage of aluminum nitrate is aluminum nitrate: 11-12wt%, ammonia water 5-6wt%, ammonium molybdate 0.2-0.3wt%, ammonium carbonate 3wt%, manganese acetate 0.7-0.8wt%, cobalt nitrate 1.5-2wt%, and H 2 O 70-72wt%。
3. The iron-cobalt based catalyst according to claim 2, wherein the iron nitrate is iron nitrate7.28wt%, aluminum nitrate: 11.3wt%, ammonia water 5.61wt%, ammonium molybdate 0.26wt%, ammonium carbonate 3wt%, manganese acetate 0.71wt%, cobalt nitrate 1.64wt%, and H 2 O 70.2wt%。
4. A preparation process of carbon nanotubes is characterized by comprising the following steps:
(1) Adding the iron-cobalt-based catalyst in the claims 1-3 into a first main reactor, then introducing nitrogen and propylene, and performing expansion cracking on the propylene under the action of the iron-cobalt-based catalyst in a nitrogen environment to obtain a carbon nanotube seed material;
(2) And blowing the carbon nano tube seed material into the second main reactor through nitrogen, and then introducing nitrogen and propylene for reaction to obtain a carbon nano tube finished product.
5. A carbon nanotube produced by the production process according to claim 4.
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Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006087590A1 (en) * 2005-02-15 2006-08-24 The Foundation Of Research And Technology Hellas / Institute Of Chemical Engineering And High Temperature Chemical Processes Catalysts for the large scale production of high purity carbon nanotubes with chemical vapor deposition
US20130171054A1 (en) * 2011-12-31 2013-07-04 Cheil Industries Inc. Supported Catalyst for Synthesizing Multi-Wall Carbon Nanotubes and Method for Preparing the Same
CN103502146A (en) * 2011-03-21 2014-01-08 阿克马法国公司 Process for fabricating carbon nanotubes and apparatus for implementing the process
US20150093576A1 (en) * 2013-09-30 2015-04-02 Samsung Sdi Co., Ltd. Carbon Nanotubes and Method for Preparing the Same
KR20160080718A (en) * 2014-12-30 2016-07-08 금호석유화학 주식회사 Method for preparing carbon nanotubes having high purity and high density
US20170022063A1 (en) * 2015-07-23 2017-01-26 Sk Innovation Co., Ltd. Catalyst for Production of Multi-Walled Carbon Nanotubes and Method of Producing Multi-Walled Carbon Nanotubes Using the Same
US20190126255A1 (en) * 2017-10-31 2019-05-02 Sk Innovation Co., Ltd. Catalyst for Synthesizing Carbon Nanotube and Method of Synthesizing Carbon Nanotube
CN110801843A (en) * 2019-11-11 2020-02-18 内蒙古骏成新能源科技有限公司 Two-stage method for preparing high-magnification carbon nano tube with superfine tube diameter, catalyst and preparation method thereof
CN113058605A (en) * 2021-03-08 2021-07-02 新奥石墨烯技术有限公司 Catalyst for carbon nanotube and preparation method and application thereof
CN114308049A (en) * 2021-12-17 2022-04-12 诺瑞(深圳)新技术有限公司 Growth catalyst for preparing carbon nano tube with high specific surface area

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006087590A1 (en) * 2005-02-15 2006-08-24 The Foundation Of Research And Technology Hellas / Institute Of Chemical Engineering And High Temperature Chemical Processes Catalysts for the large scale production of high purity carbon nanotubes with chemical vapor deposition
CN103502146A (en) * 2011-03-21 2014-01-08 阿克马法国公司 Process for fabricating carbon nanotubes and apparatus for implementing the process
US20130171054A1 (en) * 2011-12-31 2013-07-04 Cheil Industries Inc. Supported Catalyst for Synthesizing Multi-Wall Carbon Nanotubes and Method for Preparing the Same
US20150093576A1 (en) * 2013-09-30 2015-04-02 Samsung Sdi Co., Ltd. Carbon Nanotubes and Method for Preparing the Same
KR20160080718A (en) * 2014-12-30 2016-07-08 금호석유화학 주식회사 Method for preparing carbon nanotubes having high purity and high density
US20170022063A1 (en) * 2015-07-23 2017-01-26 Sk Innovation Co., Ltd. Catalyst for Production of Multi-Walled Carbon Nanotubes and Method of Producing Multi-Walled Carbon Nanotubes Using the Same
US20190126255A1 (en) * 2017-10-31 2019-05-02 Sk Innovation Co., Ltd. Catalyst for Synthesizing Carbon Nanotube and Method of Synthesizing Carbon Nanotube
CN110801843A (en) * 2019-11-11 2020-02-18 内蒙古骏成新能源科技有限公司 Two-stage method for preparing high-magnification carbon nano tube with superfine tube diameter, catalyst and preparation method thereof
CN113058605A (en) * 2021-03-08 2021-07-02 新奥石墨烯技术有限公司 Catalyst for carbon nanotube and preparation method and application thereof
CN114308049A (en) * 2021-12-17 2022-04-12 诺瑞(深圳)新技术有限公司 Growth catalyst for preparing carbon nano tube with high specific surface area

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