CN111644168A - Method for preparing atomic-scale catalyst by slowly raising temperature to greatly improve yield of hydrogen peroxide - Google Patents
Method for preparing atomic-scale catalyst by slowly raising temperature to greatly improve yield of hydrogen peroxide Download PDFInfo
- Publication number
- CN111644168A CN111644168A CN202010313678.0A CN202010313678A CN111644168A CN 111644168 A CN111644168 A CN 111644168A CN 202010313678 A CN202010313678 A CN 202010313678A CN 111644168 A CN111644168 A CN 111644168A
- Authority
- CN
- China
- Prior art keywords
- preparing
- hydrogen peroxide
- reactants
- heating
- carrying
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 title claims abstract description 36
- 239000003054 catalyst Substances 0.000 title claims abstract description 33
- 238000000034 method Methods 0.000 title claims abstract description 21
- 238000010438 heat treatment Methods 0.000 claims abstract description 42
- 238000003756 stirring Methods 0.000 claims abstract description 21
- 238000009210 therapy by ultrasound Methods 0.000 claims abstract description 21
- IEQIEDJGQAUEQZ-UHFFFAOYSA-N phthalocyanine Chemical compound N1C(N=C2C3=CC=CC=C3C(N=C3C4=CC=CC=C4C(=N4)N3)=N2)=C(C=CC=C2)C2=C1N=C1C2=CC=CC=C2C4=N1 IEQIEDJGQAUEQZ-UHFFFAOYSA-N 0.000 claims abstract description 17
- 229910052751 metal Inorganic materials 0.000 claims abstract description 11
- 229910052748 manganese Inorganic materials 0.000 claims abstract description 10
- 239000002184 metal Substances 0.000 claims abstract description 10
- 229910052725 zinc Inorganic materials 0.000 claims abstract description 10
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 5
- 239000002904 solvent Substances 0.000 claims abstract description 5
- 229910052802 copper Inorganic materials 0.000 claims abstract description 4
- 229910052742 iron Inorganic materials 0.000 claims abstract description 4
- 229910052759 nickel Inorganic materials 0.000 claims abstract description 4
- 229910052799 carbon Inorganic materials 0.000 claims abstract 3
- 239000002086 nanomaterial Substances 0.000 claims abstract 3
- 239000000376 reactant Substances 0.000 claims description 64
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 40
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 40
- 238000000137 annealing Methods 0.000 claims description 23
- 239000007789 gas Substances 0.000 claims description 21
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical group CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 20
- 229910052786 argon Inorganic materials 0.000 claims description 20
- 229910052757 nitrogen Inorganic materials 0.000 claims description 20
- 239000002245 particle Substances 0.000 claims description 20
- 230000001681 protective effect Effects 0.000 claims description 20
- 238000000967 suction filtration Methods 0.000 claims description 20
- 238000004321 preservation Methods 0.000 claims description 2
- 238000006722 reduction reaction Methods 0.000 claims 1
- 239000011259 mixed solution Substances 0.000 abstract description 20
- 239000002071 nanotube Substances 0.000 abstract description 20
- 238000011068 loading method Methods 0.000 abstract description 19
- TXEYQDLBPFQVAA-UHFFFAOYSA-N tetrafluoromethane Chemical compound FC(F)(F)F TXEYQDLBPFQVAA-UHFFFAOYSA-N 0.000 abstract description 19
- 239000002243 precursor Substances 0.000 abstract description 18
- 238000005516 engineering process Methods 0.000 abstract description 3
- 239000000463 material Substances 0.000 abstract description 2
- 150000002739 metals Chemical class 0.000 abstract description 2
- 239000000047 product Substances 0.000 abstract description 2
- 239000002994 raw material Substances 0.000 abstract description 2
- 239000011261 inert gas Substances 0.000 abstract 1
- 239000013067 intermediate product Substances 0.000 abstract 1
- 229910000510 noble metal Inorganic materials 0.000 abstract 1
- 238000002360 preparation method Methods 0.000 description 20
- 239000000243 solution Substances 0.000 description 20
- 238000001354 calcination Methods 0.000 description 19
- 238000001816 cooling Methods 0.000 description 18
- 239000012467 final product Substances 0.000 description 18
- 238000002156 mixing Methods 0.000 description 15
- 239000011572 manganese Substances 0.000 description 8
- 239000011701 zinc Substances 0.000 description 8
- MPMSMUBQXQALQI-UHFFFAOYSA-N cobalt phthalocyanine Chemical compound [Co+2].C12=CC=CC=C2C(N=C2[N-]C(C3=CC=CC=C32)=N2)=NC1=NC([C]1C=CC=CC1=1)=NC=1N=C1[C]3C=CC=CC3=C2[N-]1 MPMSMUBQXQALQI-UHFFFAOYSA-N 0.000 description 7
- KMHSUNDEGHRBNV-UHFFFAOYSA-N 2,4-dichloropyrimidine-5-carbonitrile Chemical compound ClC1=NC=C(C#N)C(Cl)=N1 KMHSUNDEGHRBNV-UHFFFAOYSA-N 0.000 description 6
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 6
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 6
- WDEQGLDWZMIMJM-UHFFFAOYSA-N benzyl 4-hydroxy-2-(hydroxymethyl)pyrrolidine-1-carboxylate Chemical compound OCC1CC(O)CN1C(=O)OCC1=CC=CC=C1 WDEQGLDWZMIMJM-UHFFFAOYSA-N 0.000 description 6
- RBTKNAXYKSUFRK-UHFFFAOYSA-N heliogen blue Chemical compound [Cu].[N-]1C2=C(C=CC=C3)C3=C1N=C([N-]1)C3=CC=CC=C3C1=NC([N-]1)=C(C=CC=C3)C3=C1N=C([N-]1)C3=CC=CC=C3C1=N2 RBTKNAXYKSUFRK-UHFFFAOYSA-N 0.000 description 6
- 239000000126 substance Substances 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 229910010272 inorganic material Inorganic materials 0.000 description 2
- 239000011147 inorganic material Substances 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Substances [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 150000004056 anthraquinones Chemical class 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000010411 electrocatalyst Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 238000001000 micrograph Methods 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 238000005381 potential energy Methods 0.000 description 1
- 238000004076 pulp bleaching Methods 0.000 description 1
- 230000027756 respiratory electron transport chain Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000007725 thermal activation Methods 0.000 description 1
- 238000011282 treatment Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
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
- 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
- B01J23/06—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of zinc, cadmium or mercury
-
- 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
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/32—Manganese, technetium or rhenium
- B01J23/34—Manganese
-
- 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
- B01J23/72—Copper
-
- 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
- B01J23/755—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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
- B01J35/33—Electric or magnetic properties
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
- C25B1/01—Products
- C25B1/28—Per-compounds
- C25B1/30—Peroxides
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B11/00—Electrodes; Manufacture thereof not otherwise provided for
- C25B11/04—Electrodes; Manufacture thereof not otherwise provided for characterised by the material
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Metallurgy (AREA)
- Inorganic Chemistry (AREA)
- Catalysts (AREA)
Abstract
The invention relates to a method for preparing an atomic-scale catalyst by slowly raising the temperature so as to greatly improve the yield of hydrogen peroxide, and belongs to the field of material science, engineering technology and chemistry. The raw materials of the catalyst prepared by the invention are phthalocyanine metal and carbon nano materials, and the related metals comprise non-noble metal elements such as Fe, Co, Ni, Mn, Cu, Zn and the like. Firstly, preparing a mixed solution A containing phthalocyanine metal and a precursor carbon fluoride nanotube in a certain load proportion, carrying out ultrasonic treatment and stirring at normal temperature to enable the mixed solution A to fully react and be uniformly loaded, removing a dispersing solvent after the loading is finished, putting a prepared intermediate product B into a tube furnace, and heating for several hours under the condition of inert gas to obtain a product C. The method has the advantages of simple operation, high efficiency, wide application range and the like. Compared with the traditional method for preparing the hydrogen peroxide, the method has the advantages of easy operation, high yield, safety, reliability and the like.
Description
Technical Field
The invention relates to a method for preparing an atomic-scale catalyst by slowly raising the temperature so as to greatly improve the yield of hydrogen peroxide, and belongs to the field of material science, engineering technology and chemistry.
Background
Hydrogen peroxide is not only a versatile and environmentally friendly chemical oxidant widely used in water treatment, pulp bleaching and chemical synthesis, but also a potential energy storage substance. Today, the large demand for hydrogen peroxide makes this chemical one of the world's important products. However, the industrial production of hydrogen peroxide was mainly based on the Riedl-Pfleideerpro (Ridel-Perdermoprol) process developed by the last 70 years, involving the sequential hydrogenation and oxidation of anthraquinones. The inherent complexity and high energy consumption of this process has prompted researchers to explore alternative processes for hydrogen peroxide production. Against this background, the development of a process for the preparation of O in alkaline medium2Partial reduction to H2O2Would be an attractive strategy, however, we are still lacking an electrocatalyst that shows high activity and selectivity, is practical and cost-effective in the production of hydrogen peroxide. Considering that the temperature is taken as an important parameter influencing the kinetics and thermodynamics of a chemical reaction, the method adopts a widely-applied catalyst preparation method and a slow heating method, controls the temperature to be increased under a gas environment, changes the bonding mode among substance elements, activates the catalytic sites of metals, and enables metal atoms to be combined with NFC to form efficient active centers at a proper thermal activation temperature to obtain the catalyst with strong ORR performance. The catalyst is in two-electron and four-electron2In the reduction way, the catalyst has stronger HOO adsorption capacity, achieves higher catalytic activity of hydrogen peroxide, and greatly improves the yield of hydrogen peroxide in electrochemical catalysis.
Disclosure of Invention
1. Objects of the invention
The invention aims to obtain a method for greatly improving the yield of hydrogen peroxide. The ORR performance of the metal catalyst and the extremely high hydrogen peroxide selectivity can be improved by a slow heating method.
2. The invention of the technology
The key points of the invention are as follows:
(1) the method comprises the steps of preparing a reactant solution A with the mass-volume concentration of 2-4mg/ml by using phthalocyanine metal, an inorganic material and a solvent, wherein metal salt elements are Fe, Co, Ni, Mn, Cu and Zn, the inorganic material is a fluorinated carbon nanotube, and the solvent is absolute ethyl alcohol.
(2) And (3) carrying out ultrasonic treatment on the solution until no particles exist, stirring for 12 hours, carrying out suction filtration, and obtaining a reactant on qualitative filter paper. After the reactant is completely dried, the obtained reactant is put in a vacuum tube furnace for calcination, nitrogen or argon is generally used as protective gas, the annealing temperature is 500-800 ℃, the annealing time is 9-14h, the heat preservation time is 1h, the heating rate is 1 ℃/min
The catalyst prepared by slowly raising the temperature improves the yield of hydrogen peroxide, and has the advantages that: the method has wide application range, can synthesize various metal catalysts such as Fe, Co, Ni, Mn, Cu, Zn and the like, has stable chemical properties, easily obtained raw materials and simple synthesis process, and can be used for large-scale production.
Drawings
FIG. 1 is a scanning transmission electron microscope image of nanotubes loaded with cobalt phthalocyanine according to the method of the present invention. FIG. 2 is a graph of hydrogen peroxide production versus electron transfer number for cobalt doped catalysts;
Detailed Description
The following describes embodiments of the method of the invention:
example 1
Preparation of 3% -800 ℃ -Co-NFC catalyst
Firstly, fully mixing cobalt phthalocyanine, carbon fluoride nanotubes and absolute ethyl alcohol, wherein the loading ratio of the cobalt phthalocyanine to a precursor is 3%, preparing a mixed solution A of 2mg/ml, carrying out ultrasonic treatment on the solution until no particles exist, stirring for 12 hours, carrying out suction filtration, and obtaining a reactant on qualitative filter paper. And after the reactants are completely dried, putting the obtained reactants into a vacuum tube furnace for calcination, generally using nitrogen or argon as protective gas, annealing at 800 ℃, keeping the temperature for 1h, heating at the rate of 1 ℃/min, and cooling to room temperature after heating is finished to obtain the final product.
Example 2
Preparation of 3% -800 ℃ -Fe-NFC catalyst
Firstly, fully mixing iron phthalocyanine, carbon fluoride nanotubes and absolute ethyl alcohol, wherein the loading ratio of the iron phthalocyanine to the precursor is 3%, preparing a mixed solution A of 2mg/ml, carrying out ultrasonic treatment on the solution until no particles exist, stirring for 12 hours, carrying out suction filtration, and obtaining a reactant on qualitative filter paper. And after the reactants are completely dried, putting the obtained reactants into a vacuum tube furnace for calcination, generally using nitrogen or argon as protective gas, annealing at 800 ℃, keeping the temperature for 1h, heating at the rate of 1 ℃/min, and cooling to room temperature after heating is finished to obtain the final product.
Example 3
Preparation of 3% -800 ℃ -Cu-NFC catalyst
Firstly, copper phthalocyanine, carbon fluoride nanotubes and absolute ethyl alcohol are fully mixed, the loading ratio of the copper phthalocyanine to a precursor is 3%, a mixed solution A of 2mg/ml is prepared, the solution is subjected to ultrasonic treatment until no particles exist, stirring is carried out for 12 hours, suction filtration is carried out, and a reactant is obtained on qualitative filter paper. And after the reactants are completely dried, putting the obtained reactants into a vacuum tube furnace for calcination, generally using nitrogen or argon as protective gas, annealing at 800 ℃, keeping the temperature for 1h, heating at the rate of 1 ℃/min, and cooling to room temperature after heating is finished to obtain the final product.
Example 4
Preparation of 3% -800 ℃ -Ni-NFC catalyst
Firstly, fully mixing nickel phthalocyanine, carbon fluoride nanotubes and absolute ethyl alcohol, wherein the loading ratio of the nickel phthalocyanine to a precursor is 3%, preparing a mixed solution A of 2mg/ml, carrying out ultrasonic treatment on the solution until no particles exist, stirring for 12 hours, carrying out suction filtration, and obtaining a reactant on qualitative filter paper. And after the reactants are completely dried, putting the obtained reactants into a vacuum tube furnace for calcination, generally using nitrogen or argon as protective gas, annealing at 800 ℃, keeping the temperature for 1h, heating at the rate of 1 ℃/min, and cooling to room temperature after heating is finished to obtain the final product.
Example 5
Preparation of 3% -800 ℃ -Zn-NFC catalyst
Firstly, fully mixing zinc phthalocyanine, carbon fluoride nanotubes and absolute ethyl alcohol, wherein the loading ratio of the zinc phthalocyanine to a precursor is 3%, preparing a mixed solution A of 2mg/ml, carrying out ultrasonic treatment on the solution until no particles exist, stirring for 12 hours, carrying out suction filtration, and obtaining a reactant on qualitative filter paper. And after the reactants are completely dried, putting the obtained reactants into a vacuum tube furnace for calcination, generally using nitrogen or argon as protective gas, annealing at 800 ℃, keeping the temperature for 1h, heating at the rate of 1 ℃/min, and cooling to room temperature after heating is finished to obtain the final product.
Example 6
Preparation of 3% -800-Mn-NFC catalyst
Firstly, fully mixing manganese phthalocyanine, carbon fluoride nanotubes and absolute ethyl alcohol, wherein the loading ratio of the manganese phthalocyanine to a precursor is 3%, preparing a mixed solution A of 2mg/ml, carrying out ultrasonic treatment on the solution until no particles exist, stirring for 12 hours, carrying out suction filtration, and obtaining a reactant on qualitative filter paper. And after the reactants are completely dried, putting the obtained reactants into a vacuum tube furnace for calcination, generally using nitrogen or argon as protective gas, annealing at 800 ℃, keeping the temperature for 1h, heating at the rate of 1 ℃/min, and cooling to room temperature after heating is finished to obtain the final product.
Example 7
Preparation of 5% -800 ℃ -Co-NFC catalyst
Firstly, fully mixing cobalt phthalocyanine, carbon fluoride nanotubes and absolute ethyl alcohol, wherein the loading ratio of the cobalt phthalocyanine to a precursor is 5%, preparing a mixed solution A of 3mg/ml, carrying out ultrasonic treatment on the solution until no particles exist, stirring for 12 hours, carrying out suction filtration, and obtaining a reactant on qualitative filter paper. And after the reactants are completely dried, putting the obtained reactants into a vacuum tube furnace for calcination, generally using nitrogen or argon as protective gas, annealing at 800 ℃, keeping the temperature for 1h, heating at the rate of 1 ℃/min, and cooling to room temperature after heating is finished to obtain the final product.
Example 8
Preparation of 5% -800 ℃ -Fe-NFC catalyst
Firstly, fully mixing iron phthalocyanine, carbon fluoride nanotubes and absolute ethyl alcohol, wherein the loading ratio of the iron phthalocyanine to the precursor is 5%, preparing a mixed solution A of 3mg/ml, carrying out ultrasonic treatment on the solution until no particles exist, stirring for 12 hours, carrying out suction filtration, and obtaining a reactant on qualitative filter paper. And after the reactants are completely dried, putting the obtained reactants into a vacuum tube furnace for calcination, generally using nitrogen or argon as protective gas, annealing at 800 ℃, keeping the temperature for 1h, heating at the rate of 1 ℃/min, and cooling to room temperature after heating is finished to obtain the final product.
Example 9
Preparation of 5% -800 ℃ -Cu-NFC catalyst
Firstly, copper phthalocyanine, carbon fluoride nanotubes and absolute ethyl alcohol are fully mixed, the loading ratio of the copper phthalocyanine to the precursor is 5%, a mixed solution A of 3mg/ml is prepared, the solution is subjected to ultrasonic treatment until no particles exist, stirring is carried out for 12 hours, suction filtration is carried out, and a reactant is obtained on qualitative filter paper. And after the reactants are completely dried, putting the obtained reactants into a vacuum tube furnace for calcination, generally using nitrogen or argon as protective gas, annealing at 800 ℃, keeping the temperature for 1h, heating at the rate of 1 ℃/min, and cooling to room temperature after heating is finished to obtain the final product.
Example 10
Preparation of 5% -800 ℃ -Zn-NFC catalyst
Firstly, fully mixing zinc phthalocyanine, carbon fluoride nanotubes and absolute ethyl alcohol, wherein the loading ratio of the zinc phthalocyanine to a precursor is 5%, preparing a mixed solution A of 3mg/ml, carrying out ultrasonic treatment on the solution until no particles exist, stirring for 12 hours, carrying out suction filtration, and obtaining a reactant on qualitative filter paper. And after the reactants are completely dried, putting the obtained reactants into a vacuum tube furnace for calcination, generally using nitrogen or argon as protective gas, annealing at 800 ℃, keeping the temperature for 1h, heating at the rate of 1 ℃/min, and cooling to room temperature after heating is finished to obtain the final product.
Example 11
Preparation of 5% -800 ℃ -Ni-NFC catalyst
Firstly, fully mixing nickel phthalocyanine, carbon fluoride nanotubes and absolute ethyl alcohol, wherein the loading ratio of the nickel phthalocyanine to a precursor is 5%, preparing a mixed solution A of 3mg/ml, carrying out ultrasonic treatment on the solution until no particles exist, stirring for 12 hours, carrying out suction filtration, and obtaining a reactant on qualitative filter paper. And after the reactants are completely dried, putting the obtained reactants into a vacuum tube furnace for calcination, generally using nitrogen or argon as protective gas, annealing at 800 ℃, keeping the temperature for 1h, heating at the rate of 1 ℃/min, and cooling to room temperature after heating is finished to obtain the final product.
Example 12
Preparation of 5% -800-Mn-NFC catalyst
Firstly, fully mixing manganese phthalocyanine, carbon fluoride nanotubes and absolute ethyl alcohol, wherein the loading capacity of the manganese phthalocyanine and a carrier is 5%, preparing a mixed solution A of 3mg/ml, carrying out ultrasonic treatment on the solution until no particles exist, stirring for 12 hours, carrying out suction filtration, and obtaining a reactant on qualitative filter paper. And after the reactants are completely dried, putting the obtained reactants into a vacuum tube furnace for calcination, generally using nitrogen or argon as protective gas, annealing at 800 ℃, keeping the temperature for 1h, heating at the rate of 1 ℃/min, and cooling to room temperature after heating is finished to obtain the final product.
Example 13
Preparation of 3% -500 ℃ -Co-NFC catalyst
Firstly, fully mixing cobalt phthalocyanine, carbon fluoride nanotubes and absolute ethyl alcohol, wherein the loading ratio of the cobalt phthalocyanine to a precursor is 3%, preparing a mixed solution A of 2mg/ml, carrying out ultrasonic treatment on the solution until no particles exist, stirring for 12 hours, carrying out suction filtration, and obtaining a reactant on qualitative filter paper. And after the reactants are completely dried, putting the obtained reactants into a vacuum tube furnace for calcination, generally using nitrogen or argon as protective gas, annealing at 800 ℃, keeping the temperature for 1h, heating at the rate of 1 ℃/min, and cooling to room temperature after heating is finished to obtain the final product.
Example 14
Preparation of 3% -500 ℃ -Fe-NFC catalyst
Firstly, fully mixing iron phthalocyanine, carbon fluoride nanotubes and absolute ethyl alcohol, wherein the loading ratio of the iron phthalocyanine to the precursor is 3%, preparing a mixed solution A of 2mg/ml, carrying out ultrasonic treatment on the solution until no particles exist, stirring for 12 hours, carrying out suction filtration, and obtaining a reactant on qualitative filter paper. And after the reactants are completely dried, putting the obtained reactants into a vacuum tube furnace for calcination, generally using nitrogen or argon as protective gas, annealing at 800 ℃, keeping the temperature for 1h, heating at the rate of 1 ℃/min, and cooling to room temperature after heating is finished to obtain the final product.
Example 15
Preparation of 3% -500 ℃ -Cu-NFC catalyst
Firstly, copper phthalocyanine, carbon fluoride nanotubes and absolute ethyl alcohol are fully mixed, the loading ratio of the copper phthalocyanine to a precursor is 3%, a mixed solution A of 2mg/ml is prepared, the solution is subjected to ultrasonic treatment until no particles exist, stirring is carried out for 12 hours, suction filtration is carried out, and a reactant is obtained on qualitative filter paper. And after the reactants are completely dried, putting the obtained reactants into a vacuum tube furnace for calcination, generally using nitrogen or argon as protective gas, annealing at 800 ℃, keeping the temperature for 1h, heating at the rate of 1 ℃/min, and cooling to room temperature after heating is finished to obtain the final product.
Example 16
Preparation of 3% -500 ℃ -Zn-NFC catalyst
Firstly, fully mixing zinc phthalocyanine, carbon fluoride nanotubes and absolute ethyl alcohol, wherein the loading ratio of the zinc phthalocyanine to a precursor is 3%, preparing a mixed solution A of 2mg/ml, carrying out ultrasonic treatment on the solution until no particles exist, stirring for 12 hours, carrying out suction filtration, and obtaining a reactant on qualitative filter paper. And after the reactants are completely dried, putting the obtained reactants into a vacuum tube furnace for calcination, generally using nitrogen or argon as protective gas, annealing at 800 ℃, keeping the temperature for 1h, heating at the rate of 1 ℃/min, and cooling to room temperature after heating is finished to obtain the final product.
Example 17
Preparation of 3% -500-Ni-NFC catalyst
Firstly, fully mixing nickel phthalocyanine, carbon fluoride nanotubes and absolute ethyl alcohol, wherein the loading ratio of the nickel phthalocyanine to a precursor is 3%, preparing a mixed solution A of 2mg/ml, carrying out ultrasonic treatment on the solution until no particles exist, stirring for 12 hours, carrying out suction filtration, and obtaining a reactant on qualitative filter paper. And after the reactants are completely dried, putting the obtained reactants into a vacuum tube furnace for calcination, generally using nitrogen or argon as protective gas, annealing at 800 ℃, keeping the temperature for 1h, heating at the rate of 1 ℃/min, and cooling to room temperature after heating is finished to obtain the final product.
Example 18
Preparation of 3% -500-Mn-NFC catalyst
Firstly, fully mixing manganese phthalocyanine, carbon fluoride nanotubes and absolute ethyl alcohol, wherein the loading ratio of the manganese phthalocyanine to a precursor is 3%, preparing a mixed solution A of 2mg/ml, carrying out ultrasonic treatment on the solution until no particles exist, stirring for 12 hours, carrying out suction filtration, and obtaining a reactant on qualitative filter paper. And after the reactants are completely dried, putting the obtained reactants into a vacuum tube furnace for calcination, generally using nitrogen or argon as protective gas, annealing at 800 ℃, keeping the temperature for 1h, heating at the rate of 1 ℃/min, and cooling to room temperature after heating is finished to obtain the final product.
Claims (1)
1. A method for preparing an atomic-scale catalyst by slowly raising the temperature so as to greatly improve the yield of hydrogen peroxide is characterized by comprising the following steps:
(1) preparing a reactant solution A of 2-4mg/ml by using phthalocyanine metal, a carbon nano material and a solvent, wherein the phthalocyanine metal elements are Fe, Co, Ni, Mn, Cu and Zn, the carbon nano material is a fluorinated carbon nano tube, and the solvent is absolute ethyl alcohol.
(2) And (3) carrying out ultrasonic treatment on the solution until no particles exist, stirring for 12 hours, carrying out suction filtration, and obtaining a reactant on qualitative filter paper.
(3) After the reactants are completely dried, the obtained reactants are put in a vacuum tube furnace for annealing, nitrogen or argon is generally used as protective gas, the annealing temperature is 500-800 ℃, the annealing time is 9-14h, the heat preservation time is 1h, the heating rate is 1 ℃/min, and the reactants are naturally cooled to the room temperature after the heating is finished.
(4) Taking out the reactant, and the obtained catalyst can be applied to O2The reduction reaction of (2) improves the yield of the hydrogen peroxide.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202010313678.0A CN111644168A (en) | 2020-04-20 | 2020-04-20 | Method for preparing atomic-scale catalyst by slowly raising temperature to greatly improve yield of hydrogen peroxide |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202010313678.0A CN111644168A (en) | 2020-04-20 | 2020-04-20 | Method for preparing atomic-scale catalyst by slowly raising temperature to greatly improve yield of hydrogen peroxide |
Publications (1)
Publication Number | Publication Date |
---|---|
CN111644168A true CN111644168A (en) | 2020-09-11 |
Family
ID=72348501
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202010313678.0A Pending CN111644168A (en) | 2020-04-20 | 2020-04-20 | Method for preparing atomic-scale catalyst by slowly raising temperature to greatly improve yield of hydrogen peroxide |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN111644168A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112619683A (en) * | 2021-01-12 | 2021-04-09 | 南开大学 | g-C co-modified by iron phthalocyanine and tungsten oxide3N4Catalyst and preparation method thereof |
CN116024601A (en) * | 2022-12-28 | 2023-04-28 | 大连理工大学 | Carbon nano tube-based porous hollow fiber electrode for electrocatalytic reduction reaction and application |
CN116237077A (en) * | 2023-03-20 | 2023-06-09 | 周口师范学院 | Method for synthesizing metal single-atom catalyst by using metal phthalocyanine compound |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU753177B2 (en) * | 1999-05-28 | 2002-10-10 | University Of Dayton, The | Patterned carbon nanotube films |
CN102027621A (en) * | 2008-04-07 | 2011-04-20 | Acta股份公司 | High performance ORR (oxygen reduction reaction) PGM (pt group metal) free catalyst |
CN102569831A (en) * | 2012-03-07 | 2012-07-11 | 东华大学 | Carbon load copper phthalocyanine fuel cell catalyst CuPc/C and preparation method and application thereof |
KR20150067975A (en) * | 2013-12-11 | 2015-06-19 | 한국수자원공사 | Manufacturing method of cathode of microbial fuel cell and cathode of microbial fuel cell manufactured by the same |
CN109390596A (en) * | 2018-09-26 | 2019-02-26 | 北京化工大学 | A kind of iron-nitrogen-C catalyst preparation method and application |
CN110911694A (en) * | 2019-11-27 | 2020-03-24 | 南方科技大学 | Method for preparing heterogeneous monomolecular electrocatalyst by using metal phthalocyanine molecule-nano carbon and application thereof |
-
2020
- 2020-04-20 CN CN202010313678.0A patent/CN111644168A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU753177B2 (en) * | 1999-05-28 | 2002-10-10 | University Of Dayton, The | Patterned carbon nanotube films |
CN102027621A (en) * | 2008-04-07 | 2011-04-20 | Acta股份公司 | High performance ORR (oxygen reduction reaction) PGM (pt group metal) free catalyst |
CN102569831A (en) * | 2012-03-07 | 2012-07-11 | 东华大学 | Carbon load copper phthalocyanine fuel cell catalyst CuPc/C and preparation method and application thereof |
KR20150067975A (en) * | 2013-12-11 | 2015-06-19 | 한국수자원공사 | Manufacturing method of cathode of microbial fuel cell and cathode of microbial fuel cell manufactured by the same |
CN109390596A (en) * | 2018-09-26 | 2019-02-26 | 北京化工大学 | A kind of iron-nitrogen-C catalyst preparation method and application |
CN110911694A (en) * | 2019-11-27 | 2020-03-24 | 南方科技大学 | Method for preparing heterogeneous monomolecular electrocatalyst by using metal phthalocyanine molecule-nano carbon and application thereof |
Non-Patent Citations (2)
Title |
---|
KUN ZHAO: ""Enhanced H2O2production by selective electrochemical reduction of O2on fluorine-doped hierarchically porous carbon"", 《JOURNAL OF CATALYSIS》 * |
谢凯: "《新一代锂二次电池技术》", 31 August 2013, 国防工业出版社 * |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112619683A (en) * | 2021-01-12 | 2021-04-09 | 南开大学 | g-C co-modified by iron phthalocyanine and tungsten oxide3N4Catalyst and preparation method thereof |
CN116024601A (en) * | 2022-12-28 | 2023-04-28 | 大连理工大学 | Carbon nano tube-based porous hollow fiber electrode for electrocatalytic reduction reaction and application |
CN116237077A (en) * | 2023-03-20 | 2023-06-09 | 周口师范学院 | Method for synthesizing metal single-atom catalyst by using metal phthalocyanine compound |
CN116237077B (en) * | 2023-03-20 | 2023-10-17 | 周口师范学院 | Method for synthesizing metal single-atom catalyst by using metal phthalocyanine compound |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN111644168A (en) | Method for preparing atomic-scale catalyst by slowly raising temperature to greatly improve yield of hydrogen peroxide | |
CN107597109A (en) | Load type gold catalyst of nano-metal-oxide doping and preparation method and application | |
CN113042085B (en) | Preparation method and application of nitrogen-phosphorus double-doped graphene-supported nickel-cobalt-palladium nano catalyst | |
CN112871198A (en) | Catalyst for synthesizing formic acid by carbon dioxide hydrogenation, preparation method and application thereof | |
CN112479317A (en) | Preparation method and application of composite cathode integrating efficient in-situ hydrogen peroxide electrosynthesis and catalytic performance | |
CN110571440B (en) | FeN4-CNT oxygen reduction catalyst preparation method | |
CN105489907B (en) | A kind of carbon nanotube loaded platinum iron superlattices alloy nano particle and preparation method thereof | |
CN114653372A (en) | Preparation method of high-dispersion nickel-based catalyst and application of high-dispersion nickel-based catalyst in catalyzing high-temperature water gas shift reaction | |
CN110828830A (en) | Self-growing carbon tube composite ZIF-8 oxygen reduction electrocatalyst | |
CN110339844B (en) | Fe nanorod and Pt @ Fe nanorod catalyst as well as synthesis and application thereof | |
CN112774690A (en) | Supported monatomic noble metal catalyst and preparation method and application thereof | |
CN110368953A (en) | A kind of composite oxide supported platinum catalyst and its preparation and application | |
CN114917932B (en) | For CO 2 Photo-reduction synthesis of CO and H 2 Catalyst, preparation method and application thereof | |
CN113976879B (en) | Carbon layer coated ferrocobalt nano core-shell structure and preparation method thereof | |
CN106140169B (en) | A kind of dimethyl ether-steam reforming hydrogen manufacturing structural catalyst and its preparation method and application | |
CN114308061B (en) | NiAu bimetallic alloy nano-catalyst and synthesis and application thereof | |
CN114686922A (en) | MOFs @ COFs catalyst with core-shell structure, preparation method thereof and application of MOFs @ COFs catalyst in electrochemical ammonia synthesis reaction | |
CN114602496A (en) | Nano-carbon-loaded platinum-iron bimetallic catalyst, preparation method thereof and application thereof in CO selective oxidation reaction under hydrogen-rich atmosphere | |
CN113842919A (en) | Catalyst for carbon dioxide hydrogenation methanation reaction and preparation method and application thereof | |
CN111659395B (en) | Preparation method and application of foamed iron-based catalyst with high all-olefin selectivity | |
CN113097499B (en) | FeNi/NiFe 2 O 4 @ NC composite material and preparation method and application thereof | |
CN115301226B (en) | Carbon nitride coated niobium cerium solid solution catalyst for reverse water gas shift reaction and preparation method thereof | |
CN116943685A (en) | Encapsulated carbon dioxide reduction catalyst and preparation method and application thereof | |
CN116190682A (en) | Transition metal monoatomic catalyst for cathodic oxygen reduction reaction and preparation method thereof | |
CN114016057A (en) | MXenes compound catalyst and preparation method and application thereof |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20200911 |