CN113101981A - Preparation method of catalyst for preparing carbon nanotube - Google Patents
Preparation method of catalyst for preparing carbon nanotube Download PDFInfo
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- CN113101981A CN113101981A CN202110370048.1A CN202110370048A CN113101981A CN 113101981 A CN113101981 A CN 113101981A CN 202110370048 A CN202110370048 A CN 202110370048A CN 113101981 A CN113101981 A CN 113101981A
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- 238000002360 preparation method Methods 0.000 title claims abstract description 77
- 239000003054 catalyst Substances 0.000 title claims abstract description 68
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 56
- 239000002041 carbon nanotube Substances 0.000 title claims abstract description 54
- 229910021393 carbon nanotube Inorganic materials 0.000 title claims abstract description 53
- SZVJSHCCFOBDDC-UHFFFAOYSA-N iron(II,III) oxide Inorganic materials O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 claims abstract description 93
- 238000006243 chemical reaction Methods 0.000 claims abstract description 68
- 238000005406 washing Methods 0.000 claims abstract description 52
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims abstract description 37
- 238000000034 method Methods 0.000 claims abstract description 35
- 239000012018 catalyst precursor Substances 0.000 claims abstract description 32
- 238000001035 drying Methods 0.000 claims abstract description 31
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 claims abstract description 29
- 238000002425 crystallisation Methods 0.000 claims abstract description 18
- 230000008025 crystallization Effects 0.000 claims abstract description 18
- VMHLLURERBWHNL-UHFFFAOYSA-M Sodium acetate Chemical compound [Na+].CC([O-])=O VMHLLURERBWHNL-UHFFFAOYSA-M 0.000 claims abstract description 15
- 238000001816 cooling Methods 0.000 claims abstract description 14
- 238000000227 grinding Methods 0.000 claims abstract description 13
- 238000000975 co-precipitation Methods 0.000 claims abstract description 12
- 239000001632 sodium acetate Substances 0.000 claims abstract description 5
- 235000017281 sodium acetate Nutrition 0.000 claims abstract description 5
- 239000007795 chemical reaction product Substances 0.000 claims abstract description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 179
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 96
- 239000000243 solution Substances 0.000 claims description 83
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 74
- 239000012266 salt solution Substances 0.000 claims description 65
- CDBYLPFSWZWCQE-UHFFFAOYSA-L sodium carbonate Substances [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 64
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 52
- 239000003513 alkali Substances 0.000 claims description 40
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 34
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 32
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 28
- 239000001257 hydrogen Substances 0.000 claims description 28
- 229910052739 hydrogen Inorganic materials 0.000 claims description 28
- 230000009467 reduction Effects 0.000 claims description 27
- 229910052786 argon Inorganic materials 0.000 claims description 26
- 239000008367 deionised water Substances 0.000 claims description 23
- 229910021641 deionized water Inorganic materials 0.000 claims description 23
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 22
- 239000011259 mixed solution Substances 0.000 claims description 22
- 238000002156 mixing Methods 0.000 claims description 22
- 238000004519 manufacturing process Methods 0.000 claims description 21
- 150000001868 cobalt Chemical class 0.000 claims description 18
- 150000002815 nickel Chemical class 0.000 claims description 18
- 230000008569 process Effects 0.000 claims description 18
- 239000012046 mixed solvent Substances 0.000 claims description 17
- 238000003756 stirring Methods 0.000 claims description 16
- 239000007789 gas Substances 0.000 claims description 14
- 150000003839 salts Chemical class 0.000 claims description 13
- 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 claims description 12
- 238000000926 separation method Methods 0.000 claims description 12
- 238000001291 vacuum drying Methods 0.000 claims description 12
- VTLYFUHAOXGGBS-UHFFFAOYSA-N Fe3+ Chemical class [Fe+3] VTLYFUHAOXGGBS-UHFFFAOYSA-N 0.000 claims description 6
- 150000001768 cations Chemical class 0.000 claims description 6
- 239000002904 solvent Substances 0.000 claims description 6
- UFMZWBIQTDUYBN-UHFFFAOYSA-N cobalt dinitrate Chemical group [Co+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O UFMZWBIQTDUYBN-UHFFFAOYSA-N 0.000 claims description 4
- 229910001981 cobalt nitrate Inorganic materials 0.000 claims description 4
- KBJMLQFLOWQJNF-UHFFFAOYSA-N nickel(ii) nitrate Chemical group [Ni+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O KBJMLQFLOWQJNF-UHFFFAOYSA-N 0.000 claims description 4
- 230000003197 catalytic effect Effects 0.000 abstract description 4
- 229910052799 carbon Inorganic materials 0.000 abstract description 2
- 230000000052 comparative effect Effects 0.000 description 14
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 8
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Substances [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 7
- 230000000694 effects Effects 0.000 description 5
- 239000002184 metal Substances 0.000 description 5
- 229910052751 metal Inorganic materials 0.000 description 5
- 239000000203 mixture Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 238000005229 chemical vapour deposition Methods 0.000 description 3
- 239000002131 composite material Substances 0.000 description 3
- GDVKFRBCXAPAQJ-UHFFFAOYSA-A dialuminum;hexamagnesium;carbonate;hexadecahydroxide Chemical compound [OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[Mg+2].[Mg+2].[Mg+2].[Mg+2].[Mg+2].[Mg+2].[Al+3].[Al+3].[O-]C([O-])=O GDVKFRBCXAPAQJ-UHFFFAOYSA-A 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 229960001545 hydrotalcite Drugs 0.000 description 3
- 229910001701 hydrotalcite Inorganic materials 0.000 description 3
- 229910002554 Fe(NO3)3·9H2O Inorganic materials 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 229910003481 amorphous carbon Inorganic materials 0.000 description 1
- 239000003990 capacitor Substances 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 229910003460 diamond Inorganic materials 0.000 description 1
- 239000010432 diamond Substances 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 239000002657 fibrous material Substances 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 238000001027 hydrothermal synthesis Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000000696 magnetic material Substances 0.000 description 1
- 230000005389 magnetism Effects 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910052750 molybdenum Inorganic materials 0.000 description 1
- 239000002048 multi walled nanotube Substances 0.000 description 1
- 239000002086 nanomaterial Substances 0.000 description 1
- 239000002071 nanotube Substances 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000012779 reinforcing material Substances 0.000 description 1
- 239000000523 sample Substances 0.000 description 1
- 239000002109 single walled nanotube Substances 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
Classifications
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/03—Precipitation; Co-precipitation
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/74—Iron group metals
- B01J23/745—Iron
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/74—Iron group metals
- B01J23/75—Cobalt
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/74—Iron group metals
- B01J23/755—Nickel
-
- 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
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/24—Nitrogen compounds
- B01J27/25—Nitrates
-
- B01J35/33—
-
- B01J35/394—
-
- B01J35/613—
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/0215—Coating
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/16—Reducing
- B01J37/18—Reducing with gases containing free hydrogen
-
- 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
Abstract
The invention relates to the technical field of carbon nanotube preparation, and discloses a preparation method of a catalyst for preparing a carbon nanotubeThe method comprises the following steps: 1) preparation of Fe3O4Magnetic core: dissolving ferric trichloride solution and sodium acetate in ethylene glycol to form solution, carrying out crystallization reaction on the solution at 200 ℃ for 8 hours, cooling, washing, separating, drying and grinding reaction products to obtain Fe3O4(ii) a 2) Preparation of the catalyst precursor: preparation of Fe by double-drop coprecipitation3O4@NiFe‑LDH、Fe3O4@ CoFe-LDH or Fe3O4@ CoFeNi-LDH catalyst precursor; 3) preparing a catalyst: reducing the catalyst precursor prepared in the step 2) in a reducing atmosphere to obtain the catalyst. The catalyst prepared by the preparation method has high catalytic activity for catalyzing the preparation of the carbon nano tube.
Description
Technical Field
The invention belongs to the technical field of carbon nanotube preparation, and particularly relates to a preparation method of a catalyst for carbon nanotube preparation.
Background
Carbon Nanotubes (CNTs) are a hollow tubular structure made of carbon elements, also known as buckytubes, which are one-dimensional quantum materials with special structures (diameters between a few nanometers to tens of nanometers, lengths up to several micrometers, and essentially sealed ends at both ends of the tube).
The carbon nano tube is used as a one-dimensional nano material, has light weight, perfect connection of a hexagonal structure and a plurality of excellent mechanical, electrical and chemical properties: 1) mechanical properties: the tensile strength of the carbon nano tube reaches 50-200 GPa, which is 100 times that of steel, the density is only 1/6 of steel, the hardness is equivalent to that of diamond, and the carbon nano tube has good flexibility and stretchability, the length-diameter ratio is generally more than 1000: 1, and the carbon nano tube is an ideal high-strength fiber material; 2) electrical properties: the carbon nano tube has the same structure as the graphite sheet structure, so the carbon nano tube has good electrical property; 3) thermal properties: the carbon nano tube has very large length-diameter ratio, so that the heat exchange performance along the length direction is very high, the carbon nano tube can synthesize a high-anisotropy heat conduction material through proper orientation, and in addition, the carbon nano tube has higher heat conductivity, so that the heat conductivity of the composite material can be greatly improved. Besides, the carbon nano tube has other good performances such as optics, hydrogen storage and the like, and the excellent performances enable the carbon nano tube to be considered as an ideal reinforcing material of the polymer composite material.
In view of the excellent physicochemical and mechanical properties of carbon nanotubes, great potential application values are receiving wide attention. The application research of the carbon nano tube mainly focuses on the fields of composite materials, hydrogen storage, electronic devices, batteries, super capacitors, field emission displays, quantum wire template electron guns, sensors, microscope probes and the like.
The preparation method of the carbon nano tube comprises the following steps: an arc method, a Chemical Vapor Deposition (CVD) method, a catalytic thermal decomposition method, a hydrothermal method, and the like, wherein the CVD method has advantages of low cost, convenient operation, and the like, and has been widely used for the preparation of CNTs. In the process of preparing the CNT, if no catalyst is added, only amorphous carbon exists in a product, and only after the catalyst is added, a product contains a large amount of single-walled carbon nanotubes and multi-walled carbon nanotubes. The catalyst is an indispensable factor for nanotube preparation.
The catalyst for preparing the carbon nano tube comprises metal simple substances and compounds, wherein the metal simple substances comprise Fe, Co, Ni, Mo, Cr, Cu, Pt and the like, and bimetallic, polymetallic and alloy can also be used as the catalyst, and the compounds comprise salts, oxides and the like of the above metals. The supported metal catalyst can well solve the problems of agglomeration, enrichment and the like of metal simple substance catalyst particles, but has the problems of low activity and unfavorable purification of the carbon nano tube.
Disclosure of Invention
In view of the above-mentioned situation existing in the prior art, the present invention aims to provide a method for preparing a catalyst for preparing carbon nanotubes by adding a magnetic material Fe3O4The catalyst prepared by combining the hydrotalcite and the hydrotalcite has higher catalytic activity when being used for preparing the carbon nano tube.
In order to achieve the purpose, the invention is realized by the following technical scheme:
the first aspect of the present invention provides a method for preparing a catalyst for carbon nanotube production, the method comprising the steps of:
1) preparation of Fe3O4Magnetic core: dissolving ferric trichloride solution and sodium acetate in ethylene glycol to form solution, carrying out crystallization reaction on the solution at 200 ℃ for 8 hours, cooling, washing, separating, drying and grinding reaction products to obtain Fe3O4;
2) Preparation of the catalyst precursor: preparation of Fe by double-drop coprecipitation3O4@NiFe-LDH、 Fe3O4@ CoFe-LDH or Fe3O4@ CoFeNi-LDH catalystA precursor;
3) preparing a catalyst: reducing the catalyst precursor prepared in the step 2) in a reducing atmosphere to obtain the catalyst.
In the present invention, Fe3O4The magnetic core may be prepared by methods conventional in the art. The method in the step 1) is preferably adopted, and specifically, the molar concentration of the ferric trichloride solution is 0.1mol/L, the molar ratio of ferric trichloride to sodium acetate is 1: 5, and the ratio of the amount of ferric trichloride to the volume of ethylene glycol is 1 mol: 10L.
Preferably, in the step 1), the crystallization reaction is completed in a reaction kettle, and the cooling is to cool the reaction kettle to 10-30 ℃ in water bath; washing with ethanol and deionized water for 2-3 times; the separation is carried out by adopting a permanent magnet in the washing process; the drying is carried out in a vacuum drying oven at 65 ℃ for 24 h.
Fe prepared by the invention3O4The magnetic core has good spherical appearance and strong magnetism.
Preferably, the Fe3O4The preparation of @ NiFe-LDH includes: mixing Fe3O4Dispersing in methanol, adding dropwise a salt solution and an alkali solution simultaneously while stirring, wherein the salt solution is a mixed solution of nickel salt and ferric iron salt, the alkali solution is a mixed solution of sodium hydroxide and sodium carbonate, the temperature is controlled at 60 ℃ and the pH value is 8-9 during the dropwise adding process, continuously crystallizing for 36h after the dropwise adding of the salt solution is finished, separating, washing, separating and drying to obtain Fe3O4@NiFe-LDH。
Further preferably, the Fe3O4The mass ratio of the methanol to the methanol is 2.5-5 g: 1L; the nickel salt is nickel nitrate, the ferric salt is ferric nitrate, the molar ratio of the nickel salt to the ferric salt is 1-3: 1, the solvent of the salt solution is a mixed solvent of methanol and water, the volume ratio of the methanol to the water is 1: 19, and the total concentration of cations in the salt solution is 0.1 mol/L; the concentration of sodium hydroxide in the alkali solution is 0.1mol/L, and the concentration of sodium carbonate is 0.2 mol/L; fe3O4The molar ratio of the nickel salt to the nickel salt is 1: 5.
Preferably, the Fe3O4Preparation of @ CoFe-LDHThe method comprises the following steps: mixing Fe3O4Dispersing in methanol, adding dropwise a salt solution and an alkali solution simultaneously while stirring, wherein the salt solution is a mixed solution of cobalt salt and ferric iron salt, the alkali solution is a mixed solution of sodium hydroxide and sodium carbonate, the temperature is controlled at 70 ℃ and the pH value is 8-8.5 during the dropwise adding process, the crystallization is continued for 36h after the dropwise adding of the salt solution is finished, and the Fe is obtained by separation, washing separation and drying3O4@CoFe-LDH。
Further preferably, the Fe3O4The mass ratio of the methanol to the methanol is 2.5-5 g: 1L; cobalt salt is cobalt nitrate, ferric salt is ferric nitrate, the molar ratio of the cobalt salt to the ferric salt is 2-5: 1, the solvent of the salt solution is a mixed solvent of methanol and water, the volume ratio of the methanol to the water is 1: 19, and the total concentration of cations in the salt solution is 0.1 mol/L; the concentration of sodium hydroxide in the alkali solution is 0.1mol/L, and the concentration of sodium carbonate is 0.2 mol/L; fe3O4The molar ratio of the cobalt salt to the cobalt salt is 1: 5.
Preferably, the Fe3O4The preparation of @ CoFeNi-LDH includes: mixing Fe3O4Dispersing in methanol, adding dropwise a salt solution and an alkali solution simultaneously while stirring, wherein the salt solution is a mixed solution of cobalt salt, nickel salt and ferric iron salt, the alkali solution is a mixed solution of sodium hydroxide and sodium carbonate, the temperature is controlled to be 60 ℃ and the pH value is 10.5 during the dropwise adding process, the crystallization is continued for 36h after the dropwise adding of the salt solution is finished, and the Fe is obtained by separation, washing separation and drying3O4@CoFeNi-LDH。
Further preferably, the Fe3O4The mass ratio of the methanol to the methanol is 2.5-5 g: 1L; the cobalt salt is cobalt nitrate, the nickel salt is nickel nitrate, the ferric salt is ferric nitrate, the molar ratio of the cobalt salt, the ferric salt and the nickel salt is 6: 3: 1, the solvent of the salt solution is a mixed solvent of methanol and water, the volume ratio of the methanol to the water is 1: 19, and the total concentration of cations in the salt solution is 0.1 mol/L; the concentration of sodium hydroxide in the alkali solution is 0.1mol/L, and the concentration of sodium carbonate is 0.2 mol/L; fe3O4The molar ratio of the cobalt salt to the total amount of the nickel salt is 1: 5.
In addition, step 2) preparation of the catalyst precursorIn the process, the separation is carried out by adopting a permanent magnet; the washing separation is to remove CO2Washing with deionized water for three times, and separating with permanent magnet in the washing process; drying is carried out at 65 ℃ for 24 hours.
The invention is realized by adding Fe3O4NiFe-LDH, CoFe-LDH and CoFeNi-LDH are coated and grown on the magnetic core, so that on one hand, the surface area of the carrier can be increased, and the dispersity of the active center is improved, thereby improving the activity of the catalyst; on the other hand, each hydrotalcite contains ions which can be used as active centers, and thus has high activity.
Preferably, in the step 3), the reducing atmosphere is a mixed gas of hydrogen and argon, the volume ratio of the hydrogen to the argon is 1: 1-20, and the reduction space velocity is 0.1-0.2hr-1(mass space velocity: mass ratio of reducing gas to catalyst precursor), the reduction temperature was 500-800 ℃.
The parameters which are not limited in the invention are the conventional parameters in the prior art.
The second aspect of the present invention provides a catalyst obtained by the above-mentioned production method.
The third aspect of the present invention provides the use of the above catalyst in the preparation of carbon nanotubes.
The catalyst prepared by the preparation method of the invention has better catalytic activity when being used for preparing the carbon nano tube.
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 any inventive step based on the embodiments of the present invention, belong to the scope of the present invention.
Example 1
A preparation method of a catalyst for preparing a carbon nanotube comprises the following steps:
1) preparation of Fe3O4Magnetic core: 8.66g FeCl was weighed3·6H2O is made to 0.1mol/L ferric trichloride solution, mixing the ferric trichloride solution with 21.77g CH3COONa·3H2Dissolving O in 320mL of glycol to form a solution, transferring the solution into a 500mL reaction kettle, carrying out crystallization reaction for 8h at 200 ℃, cooling the reaction kettle to 30 ℃ in water bath, washing the reaction kettle with ethanol and deionized water for 3 times respectively, separating the reaction kettle with a permanent magnet during washing, drying the reaction kettle for 24h at 65 ℃ in a vacuum drying oven, and grinding the reaction kettle to obtain Fe3O4;
2) Preparation of the catalyst precursor: preparation of Fe by double-drop coprecipitation3O4@ NiFe-LDH catalyst precursor, specifically, 0.87g of Fe prepared in step 1)3O4Ultrasonically dispersing in 200mL of methanol, and adding dropwise a salt solution and an alkali solution simultaneously under stirring, wherein the salt solution is prepared by adding 5.45g of Ni (NO)3)2·6H2O and 2.53gFe (NO)3)3·9H2Dissolving O in a mixed solvent of water and methanol to prepare 250mL of salt solution, wherein the volume ratio of the methanol to the water is 1: 19, dissolving sodium hydroxide and sodium carbonate in water to prepare the mixed solution, the concentration of the sodium hydroxide and the concentration of the sodium carbonate in the alkali solution are respectively 0.1mol/L and 0.2mol/L, controlling the temperature to be 60 ℃ and the pH value to be 8.5 in the dropping process, continuing to crystallize for 36h after the dropping of the salt solution is finished, separating by adopting a permanent magnet, and removing CO by adopting a CO removing method2Washing with deionized water for three times, separating with permanent magnet during washing, and drying at 65 deg.C for 24 hr to obtain Fe3O4@NiFe-LDH。
3) Preparing a catalyst: reducing the catalyst precursor prepared in the step 2) in a reducing atmosphere which is a mixed gas of hydrogen and argon, wherein the volume ratio of the hydrogen to the argon is 1: 10, and the reduction space velocity is 0.1hr-1And the reduction temperature is 600 ℃, thus obtaining the catalyst.
Example 2
A preparation method of a catalyst for preparing a carbon nanotube comprises the following steps:
1) preparation of Fe3O4Magnetic core: 8.66g FeCl was weighed3·6H2Preparing 0.1mol/L ferric trichloride solution from O, mixing the ferric trichloride solution with 21.77g CH3COONa·3H2Dissolving O in 320mL of glycol to form a solution, transferring the solution into a 500mL reaction kettle, carrying out crystallization reaction for 8h at 200 ℃, cooling the reaction kettle to 30 ℃ in water bath, washing the reaction kettle with ethanol and deionized water for 3 times respectively, separating the reaction kettle with a permanent magnet during washing, drying the reaction kettle for 24h at 65 ℃ in a vacuum drying oven, and grinding the reaction kettle to obtain Fe3O4;
2) Preparation of the catalyst precursor: preparation of Fe by double-drop coprecipitation3O4@ NiFe-LDH catalyst precursor, specifically, 0.77g of Fe prepared in step 1)3O4Ultrasonically dispersing in 200mL of methanol, and adding dropwise a salt solution of 4.85g of Ni (NO) and an alkali solution simultaneously under stirring3)2·6H2O and 3.37g Fe (NO)3)3·9H2Dissolving O in a mixed solvent of water and methanol to prepare 250mL of salt solution, wherein the volume ratio of the methanol to the water is 1: 19, dissolving sodium hydroxide and sodium carbonate in water to prepare the mixed solution, the concentration of the sodium hydroxide and the concentration of the sodium carbonate in the alkali solution are respectively 0.1mol/L and 0.2mol/L, controlling the temperature to be 60 ℃ and the pH value to be 8.5 in the dropping process, continuing to crystallize for 36h after the dropping of the salt solution is finished, separating by adopting a permanent magnet, and removing CO by adopting a CO removing method2Washing with deionized water for three times, separating with permanent magnet during washing, and drying at 65 deg.C for 24 hr to obtain Fe3O4@NiFe-LDH。
3) Preparing a catalyst: reducing the catalyst precursor prepared in the step 2) in a reducing atmosphere which is a mixed gas of hydrogen and argon, wherein the volume ratio of the hydrogen to the argon is 1: 20, and the reduction space velocity is 0.2hr-1The reduction temperature was 650 ℃ to obtain a catalyst.
Example 3
A preparation method of a catalyst for preparing a carbon nanotube comprises the following steps:
1) preparation of Fe3O4Magnetic core: 8.66g FeCl was weighed3·6H2Preparing 0.1mol/L ferric trichloride solution from O, mixing the ferric trichloride solution with 21.77g CH3COONa·3H2Dissolving O in 320mL of glycol to form a solution, and transferring the solution into a 500mL reaction kettlePerforming crystallization reaction at 200 ℃ for 8h, cooling the reaction kettle to 20 ℃ in water bath, washing with ethanol and deionized water for 3 times respectively, separating with a permanent magnet in the washing process, drying in a vacuum drying oven at 65 ℃ for 24h, and grinding to obtain Fe3O4;
2) Preparation of the catalyst precursor: preparation of Fe by double-drop coprecipitation3O4@ NiFe-LDH catalyst precursor, specifically, 0.58g of Fe prepared in step 1)3O4Ultrasonically dispersing in 200mL of methanol, and adding dropwise a salt solution of 3.63g of Ni (NO) and an alkali solution simultaneously under stirring3)2·6H2O and 5.05g Fe (NO)3)3·9H2Dissolving O in a mixed solvent of water and methanol to prepare 250mL of salt solution, wherein the volume ratio of the methanol to the water is 1: 19, dissolving sodium hydroxide and sodium carbonate in water to prepare the mixed solution, the concentration of the sodium hydroxide and the concentration of the sodium carbonate in the alkali solution are respectively 0.1mol/L and 0.2mol/L, controlling the temperature to be 60 ℃ and the pH value to be 9 in the dropping process, continuing to crystallize for 36h after the dropping of the salt solution is finished, separating by adopting a permanent magnet, and removing CO by adopting a CO removing method2Washing with deionized water for three times, separating with permanent magnet during washing, and drying at 65 deg.C for 24 hr to obtain Fe3O4@NiFe-LDH。
3) Preparing a catalyst: reducing the catalyst precursor prepared in the step 2) in a reducing atmosphere, wherein the reducing atmosphere is a mixed gas of hydrogen and argon, the volume ratio of the hydrogen to the argon is 1: 1, and the reduction space velocity is 0.15hr-1And the reduction temperature is 700 ℃, thus obtaining the catalyst.
Example 4
A preparation method of a catalyst for preparing a carbon nanotube comprises the following steps:
1) preparation of Fe3O4Magnetic core: 8.66g FeCl was weighed3·6H2Preparing 0.1mol/L ferric trichloride solution from O, mixing the ferric trichloride solution with 21.77g CH3COONa·3H2Dissolving O in 320mL of ethylene glycol to form a solution, transferring the solution into a 500mL reaction kettle, performing crystallization reaction at 200 ℃ for 8 hours, cooling the reaction kettle to 30 ℃ in water bath, and removing by using ethanolWashing with water for 2 times, separating with permanent magnet, drying at 65 deg.C for 24 hr in vacuum drying oven, and grinding to obtain Fe3O4;
2) Preparation of the catalyst precursor: preparation of Fe by double-drop coprecipitation3O4@ CoFe-LDH catalyst precursor, specifically, 0.77g of Fe prepared in step 1)3O4Ultrasonically dispersing in 200mL of methanol, and adding dropwise a salt solution and an alkali solution simultaneously under stirring, wherein the salt solution is prepared by adding 4.85g of Co (NO)3)2·6H2O and 3.37g Fe (NO)3)3·9H2Dissolving O in a mixed solvent of water and methanol to prepare 250mL of salt solution, wherein the volume ratio of the methanol to the water is 1: 19, dissolving sodium hydroxide and sodium carbonate in water to prepare the mixed solution, the concentration of the sodium hydroxide and the concentration of the sodium carbonate in the alkali solution are respectively 0.1mol/L and 0.2mol/L, controlling the temperature to be 70 ℃ and the pH value to be 8 in the dropping process, continuing to crystallize for 36h after the dropping of the salt solution is finished, separating by adopting a permanent magnet, and removing CO by adopting a CO removing method2Washing with deionized water for three times, separating with permanent magnet during washing, and drying at 65 deg.C for 24 hr to obtain Fe3O4@CoFe-LDH。
3) Preparing a catalyst: reducing the catalyst precursor prepared in the step 2) in a reducing atmosphere which is a mixed gas of hydrogen and argon, wherein the volume ratio of the hydrogen to the argon is 1: 1, and the reduction space velocity is 0.1hr-1And the reduction temperature is 700 ℃, thus obtaining the catalyst.
Example 5
A preparation method of a catalyst for preparing a carbon nanotube comprises the following steps:
1) preparation of Fe3O4Magnetic core: 8.66g FeCl was weighed3·6H2Preparing 0.1mol/L ferric trichloride solution from O, mixing the ferric trichloride solution with 21.77g CH3COONa·3H2Dissolving O in 320mL of ethylene glycol to form a solution, transferring the solution into a 500mL reaction kettle, carrying out crystallization reaction for 8h at 200 ℃, cooling the reaction kettle to 30 ℃ in water bath, washing with ethanol and deionized water for 3 times respectively, separating by using a permanent magnet in the washing process, and drying in vacuumDrying in a box at 65 ℃ for 24h, and grinding to obtain Fe3O4;
2) Preparation of the catalyst precursor: preparation of Fe by double-drop coprecipitation3O4@ CoFe-LDH catalyst precursor, specifically, 0.87g of Fe prepared in step 1)3O4Ultrasonically dispersing in 200mL of methanol, and adding dropwise a salt solution and an alkali solution simultaneously under stirring, wherein the salt solution is prepared by adding 5.46g of Co (NO)3)2·6H2O and 2.53g Fe (NO)3)3·9H2Dissolving O in a mixed solvent of water and methanol to prepare 250mL of salt solution, wherein the volume ratio of the methanol to the water is 1: 19, dissolving sodium hydroxide and sodium carbonate in water to prepare the mixed solution, the concentration of the sodium hydroxide and the concentration of the sodium carbonate in the alkali solution are respectively 0.1mol/L and 0.2mol/L, controlling the temperature to be 70 ℃ and the pH value to be 8.2 in the dropping process, continuing to crystallize for 36h after the dropping of the salt solution is finished, separating by adopting a permanent magnet, and removing CO by adopting a CO removing method2Washing with deionized water for three times, separating with permanent magnet during washing, and drying at 65 deg.C for 24 hr to obtain Fe3O4@CoFe-LDH。
3) Preparing a catalyst: reducing the catalyst precursor prepared in the step 2) in a reducing atmosphere which is a mixed gas of hydrogen and argon, wherein the volume ratio of the hydrogen to the argon is 1: 10, and the reduction space velocity is 0.2hr-1And the reduction temperature is 750 ℃, thus obtaining the catalyst.
Example 6
A preparation method of a catalyst for preparing a carbon nanotube comprises the following steps:
1) preparation of Fe3O4Magnetic core: 8.66g FeCl was weighed3·6H2Preparing 0.1mol/L ferric trichloride solution from O, mixing the ferric trichloride solution with 21.77g CH3COONa·3H2Dissolving O in 320mL of glycol to form a solution, transferring the solution into a 500mL reaction kettle, carrying out crystallization reaction for 8h at 200 ℃, cooling the reaction kettle to 20 ℃ in water bath, washing the reaction kettle with ethanol and deionized water for 3 times respectively, separating the reaction kettle with a permanent magnet during washing, drying the reaction kettle for 24h at 65 ℃ in a vacuum drying oven, and grinding the reaction kettle to obtain Fe3O4;
2) Preparation of the catalyst precursor: preparation of Fe by double-drop coprecipitation3O4@ CoFe-LDH catalyst precursor, specifically, 0.96g of Fe prepared in step 1)3O4Ultrasonically dispersing in 200mL of methanol, and adding dropwise a salt solution and an alkali solution simultaneously under stirring, wherein the salt solution is prepared by adding 6.06g of Co (NO)3)2·6H2O and 1.68g Fe (NO)3)3·9H2Dissolving O in a mixed solvent of water and methanol to prepare 250mL of salt solution, wherein the volume ratio of the methanol to the water is 1: 19, dissolving sodium hydroxide and sodium carbonate in water to prepare the mixed solution, the concentration of the sodium hydroxide and the concentration of the sodium carbonate in the alkali solution are respectively 0.1mol/L and 0.2mol/L, controlling the temperature to be 70 ℃ and the pH value to be 8.5 in the dropping process, continuing to crystallize for 36h after the dropping of the salt solution is finished, separating by adopting a permanent magnet, and removing CO by adopting a CO removing method2Washing with deionized water for three times, separating with permanent magnet during washing, and drying at 65 deg.C for 24 hr to obtain Fe3O4@CoFe-LDH。
3) Preparing a catalyst: reducing the catalyst precursor prepared in the step 2) in a reducing atmosphere which is a mixed gas of hydrogen and argon, wherein the volume ratio of the hydrogen to the argon is 1: 20, and the reduction space velocity is 0.2hr-1And the reduction temperature is 800 ℃, thus obtaining the catalyst.
Example 7
A preparation method of a catalyst for preparing a carbon nanotube comprises the following steps:
1) preparation of Fe3O4Magnetic core: 8.66g FeCl was weighed3·6H2Preparing 0.1mol/L ferric trichloride solution from O, mixing the ferric trichloride solution with 21.77g CH3COONa·3H2Dissolving O in 320mL of glycol to form a solution, transferring the solution into a 500mL reaction kettle, carrying out crystallization reaction for 8h at 200 ℃, cooling the reaction kettle to 30 ℃ in water bath, washing the reaction kettle with ethanol and deionized water for 2 times respectively, separating the reaction kettle with a permanent magnet during washing, drying the reaction kettle for 24h at 65 ℃ in a vacuum drying oven, and grinding the reaction kettle to obtain Fe3O4;
2) Preparation of the catalyst precursor: by two-drop co-precipitationMethod for preparing Fe3O4@ CoFeNi-LDH catalyst precursor, specifically, 0.81g of Fe prepared in step 1)3O4Ultrasonically dispersing in 200mL of methanol, and adding dropwise a salt solution and an alkali solution simultaneously under stirring, wherein the salt solution is prepared by adding 4.37g of Co (NO)3)2·6H2O、3.03g Fe(NO3)3·9H2O and 0.73g Ni (NO)3)2·6H2Dissolving O in a mixed solvent of water and methanol to prepare 250mL of salt solution, wherein the volume ratio of the methanol to the water is 1: 19, dissolving sodium hydroxide and sodium carbonate in water to prepare the mixed solution, the concentration of the sodium hydroxide and the concentration of the sodium carbonate in the alkali solution are respectively 0.1mol/L and 0.2mol/L, controlling the temperature at 60 ℃ and the pH value at 10.5 in the dropping process, continuing to crystallize for 36h after the dropping of the salt solution is finished, separating by using a permanent magnet, removing CO by using a CO removal method2Washing with deionized water for three times, separating with permanent magnet during washing, and drying at 65 deg.C for 24 hr to obtain Fe3O4@CoFeNi-LDH。
3) Preparing a catalyst: reducing the catalyst precursor prepared in the step 2) in a reducing atmosphere which is a mixed gas of hydrogen and argon, wherein the volume ratio of the hydrogen to the argon is 1: 10, and the reduction space velocity is 0.1hr-1And the reduction temperature is 700 ℃, thus obtaining the catalyst.
Comparative example 1
1) Preparation of Fe3O4Magnetic core: 8.66g FeCl was weighed3·6H2Preparing 0.1mol/L ferric trichloride solution from O, mixing the ferric trichloride solution with 21.77g CH3COONa·3H2Dissolving O in 320mL of glycol to form a solution, transferring the solution into a 500mL reaction kettle, carrying out crystallization reaction for 8h at 200 ℃, cooling the reaction kettle to 30 ℃ in water bath, washing the reaction kettle with ethanol and deionized water for 2 times respectively, separating the reaction kettle with a permanent magnet during washing, drying the reaction kettle for 24h at 65 ℃ in a vacuum drying oven, and grinding the reaction kettle to obtain Fe3O4。
2) Preparation of NiFe-LDH catalyst precursor by two-drop coprecipitation with Fe in example 13O4The preparation of @ NiFe-LDH differs: does not contain Fe3O4The step of (2) dispersing the dispersion,while stirring, a salt solution prepared by adding 5.45g of Ni (NO) and an alkali solution simultaneously dropwise directly to 200mL of methanol3)2·6H2O and 2.53g Fe (NO)3)3·9H2Dissolving O in a mixed solvent of water and methanol to prepare 250mL of salt solution, wherein the volume ratio of the methanol to the water is 1: 19, dissolving sodium hydroxide and sodium carbonate in the aqueous alkali to prepare the mixed solution, the concentration of the sodium hydroxide and the concentration of the sodium carbonate in the aqueous alkali are respectively 0.1mol/L and 0.2mol/L, controlling the temperature at 60 ℃ and the pH value at 8.5 in the dropping process, continuing to crystallize for 36h after the dropping of the salt solution is finished, filtering and separating, and removing CO by adopting2Washing with deionized water for three times, and drying at 65 ℃ for 24 hours to obtain NiFe-LDH.
3) 0.87g of Fe obtained in step 1)3O4Mixing with NiFe-LDH prepared in step 2), and reducing the mixture in reducing atmosphere of mixed gas of hydrogen and argon at volume ratio of 1: 10 and space velocity of 0.1hr-1The reduction temperature was 600 ℃ to obtain comparative catalyst 1.
Comparative example 2
Fe obtained in step 1) of comparative example 13O40.87g is reduced in a reducing atmosphere which is a mixed gas of hydrogen and argon, the volume ratio of the hydrogen to the argon is 1: 10, and the reduction space velocity is 0.1hr-1The reduction temperature was 600 ℃ to obtain comparative catalyst 2.
Comparative example 3
Reducing the NiFe-LDH prepared in the step 2) in the comparative example 1 in a reducing atmosphere which is a mixed gas of hydrogen and argon, wherein the volume ratio of the hydrogen to the argon is 1: 10, and the reduction space velocity is 0.1hr-1The reduction temperature was 600 ℃ to obtain comparative catalyst 3.
Comparative example 4
1) Preparation of Fe3O4Magnetic core: 8.66g FeCl was weighed3·6H2Preparing 0.1mol/L ferric trichloride solution from O, mixing the ferric trichloride solution with 21.77g CH3COONa·3H2Dissolving O in 320mL of glycol to form a solution, transferring the solution into a 500mL reaction kettle, performing crystallization reaction at 200 ℃ for 8h, and reactingCooling the reaction kettle to 30 ℃ in water bath, washing the reaction kettle for 2 times by using ethanol and deionized water respectively, separating the reaction kettle by using a permanent magnet in the washing process, drying the reaction kettle for 24 hours at 65 ℃ in a vacuum drying oven, and grinding the reaction kettle to obtain Fe3O4。
2) Preparation of CoFe-LDH catalyst precursor by two-drop coprecipitation with Fe in example 43O4The preparation of @ CoFe-LDH differs: does not contain Fe3O4The dispersing step of (1), adding dropwise to 200mL of methanol, while stirring, a salt solution prepared by mixing 4.85g of Co (NO) and an alkali solution3)2·6H2O and 3.37g Fe (NO)3)3·9H2Dissolving O in a mixed solvent of water and methanol to prepare 250mL of salt solution, wherein the volume ratio of the methanol to the water is 1: 19, dissolving sodium hydroxide and sodium carbonate in the aqueous alkali to prepare the mixed solution, the concentration of the sodium hydroxide and the concentration of the sodium carbonate in the aqueous alkali are respectively 0.1mol/L and 0.2mol/L, controlling the temperature to be 70 ℃ and the pH value to be 8 in the dropping process, continuing to crystallize for 36h after the dropping of the salt solution is finished, filtering and separating, and removing CO by adopting2Washed three times with deionized water and dried for 24 hours at 65 ℃ to obtain CoFe-LDH.
3) 0.77g of Fe obtained in step 1)3O4Mixing with CoFe-LDH prepared in step 2), and reducing the mixture in a reducing atmosphere of a mixture of hydrogen and argon at a volume ratio of 1: 1 and a reduction space velocity of 0.1hr-1The reduction temperature was 700 ℃ to obtain comparative catalyst 4.
Comparative example 5
1) Preparation of Fe3O4Magnetic core: 8.66g FeCl was weighed3·6H2Preparing 0.1mol/L ferric trichloride solution from O, mixing the ferric trichloride solution with 21.77g CH3COONa·3H2Dissolving O in 320mL of glycol to form a solution, transferring the solution into a 500mL reaction kettle, carrying out crystallization reaction for 8h at 200 ℃, cooling the reaction kettle to 30 ℃ in water bath, washing the reaction kettle with ethanol and deionized water for 2 times respectively, separating the reaction kettle with a permanent magnet during washing, drying the reaction kettle for 24h at 65 ℃ in a vacuum drying oven, and grinding the reaction kettle to obtain Fe3O4。
2) Preparation of CoFeNi-LDH by two-drop coprecipitation with Fe in example 73O4The preparation of @ CoFeNi-LDH differs in that: does not contain Fe3O4The dispersing step of (1), to 200mL of methanol were added dropwise, simultaneously, with stirring, a salt solution obtained by mixing 4.37g of Co (NO)3)2·6H2O、3.03g Fe(NO3)3·9H2O and 0.73g Ni (NO)3)2·6H2Dissolving O in a mixed solvent of water and methanol to prepare 250mL of salt solution, wherein the volume ratio of the methanol to the water is 1: 19, dissolving sodium hydroxide and sodium carbonate in the aqueous alkali to prepare the mixed solution, the concentration of the sodium hydroxide and the concentration of the sodium carbonate in the aqueous alkali are respectively 0.1mol/L and 0.2mol/L, controlling the temperature at 60 ℃ and the pH value at 10.5 in the dropping process, continuing to crystallize for 36h after the dropping of the salt solution is finished, filtering and separating, and removing CO by adopting2Washed three times by deionized water, and dried for 24 hours at 65 ℃ to obtain CoFeNi-LDH.
3) 0.81g of Fe obtained in step 1)3O4Mixing with the CoFeNi-LDH prepared in the step 2), and reducing the mixture in a reducing atmosphere which is a mixed gas of hydrogen and argon, wherein the volume ratio of the hydrogen to the argon is 1: 10, and the reduction space velocity is 0.1hr-1The reduction temperature was 700 ℃ to obtain comparative catalyst 5.
Application examples 1 to 7
The catalysts prepared in examples 1 to 7 were used for the preparation of carbon nanotubes, respectively, and it should be noted that the step 3) of the catalyst preparation was performed in a carbon nanotube preparing apparatus, and the reaction conditions were controlled. The conditions for the preparation of carbon nanotubes and the parameters for the preparation of carbon nanotubes are shown in table 1.
Application of comparative examples 1 to 5
The catalysts prepared in comparative examples 1 to 5 were used for the preparation of carbon nanotubes, respectively, and it should be noted that the step 3) of the preparation of the catalysts was performed in a carbon nanotube preparing apparatus, and the preparation conditions were controlled. The conditions for the preparation of carbon nanotubes and the parameters for the preparation of carbon nanotubes are shown in table 1.
TABLE 1
As can be seen from the data in Table 1, the present invention is achieved by adding Fe3O4NiFe-LDH, CoFe-LDH and CoFeNi-LDH are coated and grown on the magnetic core, which can improve the activity of the catalyst and Fe3O4Compared with the simple mixing of magnetic cores and LDH, the activity of the catalyst obtained by corresponding coating production is higher, which proves that Fe3O4The magnetic core and the LDH have a synergistic effect.
Having described embodiments of the present invention, the foregoing description is intended to be exemplary, not exhaustive, and not limited to the disclosed embodiments. Many modifications and variations will be apparent to those of ordinary skill in the art without departing from the scope and spirit of the illustrated embodiments.
Claims (10)
1. The preparation method of the catalyst for preparing the carbon nanotube is characterized by comprising the following steps: the preparation method comprises the following steps:
1) preparation of Fe3O4Magnetic core: dissolving ferric trichloride solution and sodium acetate in ethylene glycol to form solution, carrying out crystallization reaction on the solution at 200 ℃ for 8 hours, cooling, washing, separating, drying and grinding reaction products to obtain Fe3O4;
2) Preparation of the catalyst precursor: preparation of Fe by double-drop coprecipitation3O4@NiFe-LDH、Fe3O4@ CoFe-LDH or Fe3O4@ CoFeNi-LDH catalyst precursor;
3) preparing a catalyst: reducing the catalyst precursor prepared in the step 2) in a reducing atmosphere to obtain the catalyst.
2. The method for producing a catalyst for carbon nanotube production according to claim 1, wherein: the molar concentration of the ferric trichloride solution is 0.1mol/L, the molar ratio of the ferric trichloride to the sodium acetate is 1: 5, and the volume ratio of the amount of the ferric trichloride to the volume of the ethylene glycol is 1 mol: 10L;
in the step 1), the crystallization reaction is finished in a reaction kettle, and the cooling is to cool the reaction kettle to 10-30 ℃ in water bath; washing with ethanol and deionized water for 2-3 times; the separation is carried out by adopting a permanent magnet in the washing process; the drying is carried out in a vacuum drying oven at 65 ℃ for 24 h.
3. The method for producing a catalyst for carbon nanotube production according to claim 1, wherein: said Fe3O4The preparation of @ NiFe-LDH includes: mixing Fe3O4Dispersing in methanol, adding dropwise a salt solution and an alkali solution simultaneously while stirring, wherein the salt solution is a mixed solution of nickel salt and ferric iron salt, the alkali solution is a mixed solution of sodium hydroxide and sodium carbonate, the temperature is controlled at 60 ℃ and the pH value is 8-9 during the dropwise adding process, continuously crystallizing for 36h after the dropwise adding of the salt solution is finished, separating, washing, separating and drying to obtain Fe3O4@NiFe-LDH。
4. The method for producing a catalyst for carbon nanotube production according to claim 3, wherein: said Fe3O4The mass ratio of the methanol to the methanol is 2.5-5 g: 1L; the nickel salt is nickel nitrate, the ferric salt is ferric nitrate, the molar ratio of the nickel salt to the ferric salt is 1-3: 1, the solvent of the salt solution is a mixed solvent of methanol and water, the volume ratio of the methanol to the water is 1: 19, and the total concentration of cations in the salt solution is 0.1 mol/L; the concentration of sodium hydroxide in the alkali solution is 0.1mol/L, and the concentration of sodium carbonate is 0.2 mol/L; fe3O4The molar ratio of the nickel salt to the nickel salt is 1: 5.
5. The method for producing a catalyst for carbon nanotube production according to claim 1, wherein: said Fe3O4The preparation of @ CoFe-LDH includes: mixing Fe3O4Dispersing in methanol, stirring, addingSimultaneously dripping a salt solution and an alkali solution, wherein the salt solution is a mixed solution of cobalt salt and ferric iron salt, the alkali solution is a mixed solution of sodium hydroxide and sodium carbonate, controlling the temperature to be 70 ℃ and the pH value to be 8-8.5 in the dripping process, continuously crystallizing for 36 hours after the dripping of the salt solution is finished, separating, washing, separating and drying to obtain Fe3O4@CoFe-LDH。
6. The method for producing a catalyst for carbon nanotube production according to claim 5, wherein: said Fe3O4The mass ratio of the methanol to the methanol is 2.5-5 g: 1L; cobalt salt is cobalt nitrate, ferric salt is ferric nitrate, the molar ratio of the cobalt salt to the ferric salt is 2-5: 1, the solvent of the salt solution is a mixed solvent of methanol and water, the volume ratio of the methanol to the water is 1: 19, and the total concentration of cations in the salt solution is 0.1 mol/L; the concentration of sodium hydroxide in the alkali solution is 0.1mol/L, and the concentration of sodium carbonate is 0.2 mol/L; fe3O4The molar ratio of the cobalt salt to the cobalt salt is 1: 5.
7. The method for producing a catalyst for carbon nanotube production according to claim 1, wherein: said Fe3O4The preparation of @ CoFeNi-LDH includes: mixing Fe3O4Dispersing in methanol, adding dropwise a salt solution and an alkali solution simultaneously while stirring, wherein the salt solution is a mixed solution of cobalt salt, nickel salt and ferric iron salt, the alkali solution is a mixed solution of sodium hydroxide and sodium carbonate, the temperature is controlled to be 60 ℃ and the pH value is 10.5 during the dropwise adding process, the crystallization is continued for 36h after the dropwise adding of the salt solution is finished, and the Fe is obtained by separation, washing separation and drying3O4@CoFeNi-LDH。
8. The method for producing a catalyst for carbon nanotube production according to claim 7, wherein: said Fe3O4The mass ratio of the methanol to the methanol is 2.5-5 g: 1L; cobalt salt is cobalt nitrate, nickel salt is nickel nitrate, ferric salt is ferric nitrate, the molar ratio of cobalt salt, ferric salt and nickel salt is 6: 3: 1, the solvent of salt solution is the mixed solvent of methanol and water, the mixed solvent of methanol and waterThe volume ratio is 1: 19, and the total concentration of cations in the salt solution is 0.1 mol/L; the concentration of sodium hydroxide in the alkali solution is 0.1mol/L, and the concentration of sodium carbonate is 0.2 mol/L; fe3O4The molar ratio of the cobalt salt to the total amount of the nickel salt is 1: 5.
9. The method for producing a catalyst for production of a carbon nanotube according to claim 3, 5 or 7, characterized in that: in the step 2), the separation is carried out by adopting a permanent magnet; the washing separation is to remove CO2Washing with deionized water for three times, and separating with permanent magnet in the washing process; drying is carried out at 65 ℃ for 24 hours.
10. The method for producing a catalyst for carbon nanotube production according to claim 1, wherein: in step 3), the reducing atmosphere is a mixed gas of hydrogen and argon, the volume ratio of hydrogen to argon is 1: 1-20, and the reduction space velocity is 0.1-0.2hr-1The reduction temperature is 500-800 ℃.
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