CN116695170A - Preparation method of Zn-doped Bi2O3 bimetallic catalyst - Google Patents
Preparation method of Zn-doped Bi2O3 bimetallic catalyst Download PDFInfo
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- 239000003054 catalyst Substances 0.000 title claims abstract description 53
- 238000002360 preparation method Methods 0.000 title claims abstract description 22
- WMWLMWRWZQELOS-UHFFFAOYSA-N bismuth(iii) oxide Chemical compound O=[Bi]O[Bi]=O WMWLMWRWZQELOS-UHFFFAOYSA-N 0.000 title description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims abstract description 40
- 229910015902 Bi 2 O 3 Inorganic materials 0.000 claims abstract description 22
- 229910002092 carbon dioxide Inorganic materials 0.000 claims abstract description 20
- 239000001569 carbon dioxide Substances 0.000 claims abstract description 20
- 238000001035 drying Methods 0.000 claims abstract description 16
- 239000011701 zinc Substances 0.000 claims abstract description 16
- YSWBFLWKAIRHEI-UHFFFAOYSA-N 4,5-dimethyl-1h-imidazole Chemical compound CC=1N=CNC=1C YSWBFLWKAIRHEI-UHFFFAOYSA-N 0.000 claims abstract description 12
- 238000000137 annealing Methods 0.000 claims abstract description 12
- XIOUDVJTOYVRTB-UHFFFAOYSA-N 1-(1-adamantyl)-3-aminothiourea Chemical compound C1C(C2)CC3CC2CC1(NC(=S)NN)C3 XIOUDVJTOYVRTB-UHFFFAOYSA-N 0.000 claims abstract description 8
- 239000000243 solution Substances 0.000 claims description 25
- 238000000034 method Methods 0.000 claims description 11
- 150000001621 bismuth Chemical class 0.000 claims description 10
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 claims description 8
- 239000012266 salt solution Substances 0.000 claims description 8
- 150000003751 zinc Chemical class 0.000 claims description 8
- FBXVOTBTGXARNA-UHFFFAOYSA-N bismuth;trinitrate;pentahydrate Chemical group O.O.O.O.O.[Bi+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O FBXVOTBTGXARNA-UHFFFAOYSA-N 0.000 claims description 7
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 5
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 claims description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 4
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 4
- 235000019253 formic acid Nutrition 0.000 claims description 4
- 239000012265 solid product Substances 0.000 claims description 4
- 238000002156 mixing Methods 0.000 claims description 2
- 239000002904 solvent Substances 0.000 claims description 2
- 230000000630 rising effect Effects 0.000 claims 1
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 abstract description 36
- 239000000047 product Substances 0.000 abstract description 17
- 238000003756 stirring Methods 0.000 abstract description 11
- 230000003197 catalytic effect Effects 0.000 abstract description 6
- 239000007795 chemical reaction product Substances 0.000 abstract description 6
- 239000007788 liquid Substances 0.000 abstract description 6
- 239000007787 solid Substances 0.000 abstract description 6
- 238000006555 catalytic reaction Methods 0.000 abstract description 5
- 239000002086 nanomaterial Substances 0.000 abstract description 2
- RXPAJWPEYBDXOG-UHFFFAOYSA-N hydron;methyl 4-methoxypyridine-2-carboxylate;chloride Chemical compound Cl.COC(=O)C1=CC(OC)=CC=N1 RXPAJWPEYBDXOG-UHFFFAOYSA-N 0.000 abstract 1
- 238000006722 reduction reaction Methods 0.000 description 8
- 230000009467 reduction Effects 0.000 description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- 229910052799 carbon Inorganic materials 0.000 description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 239000011259 mixed solution Substances 0.000 description 4
- 239000004744 fabric Substances 0.000 description 3
- KJCVRFUGPWSIIH-UHFFFAOYSA-N 1-naphthol Chemical compound C1=CC=C2C(O)=CC=CC2=C1 KJCVRFUGPWSIIH-UHFFFAOYSA-N 0.000 description 2
- 229910007563 Zn—Bi Inorganic materials 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 230000001699 photocatalysis Effects 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 229910021607 Silver chloride Inorganic materials 0.000 description 1
- HUSDWXLHMHIZOW-UHFFFAOYSA-N [Zn].O=C=O Chemical compound [Zn].O=C=O HUSDWXLHMHIZOW-UHFFFAOYSA-N 0.000 description 1
- 230000001476 alcoholic effect Effects 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910000416 bismuth oxide Inorganic materials 0.000 description 1
- 238000010531 catalytic reduction reaction Methods 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- TYIXMATWDRGMPF-UHFFFAOYSA-N dibismuth;oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[Bi+3].[Bi+3] TYIXMATWDRGMPF-UHFFFAOYSA-N 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000000840 electrochemical analysis Methods 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 238000004817 gas chromatography Methods 0.000 description 1
- 239000005431 greenhouse gas Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002064 nanoplatelet Substances 0.000 description 1
- 239000002135 nanosheet Substances 0.000 description 1
- 230000005311 nuclear magnetism Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000007146 photocatalysis Methods 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000004626 scanning electron microscopy Methods 0.000 description 1
- HKZLPVFGJNLROG-UHFFFAOYSA-M silver monochloride Chemical compound [Cl-].[Ag+] HKZLPVFGJNLROG-UHFFFAOYSA-M 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 238000013112 stability test Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 238000004627 transmission electron microscopy Methods 0.000 description 1
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/8671—Removing components of defined structure not provided for in B01D53/8603 - B01D53/8668
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- 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
- C25B1/23—Carbon monoxide or syngas
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- 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
- C25B11/051—Electrodes formed of electrocatalysts on a substrate or carrier
- C25B11/055—Electrodes formed of electrocatalysts on a substrate or carrier characterised by the substrate or carrier material
- C25B11/057—Electrodes formed of electrocatalysts on a substrate or carrier characterised by the substrate or carrier material consisting of a single element or compound
- C25B11/065—Carbon
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- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
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- C25B11/04—Electrodes; Manufacture thereof not otherwise provided for characterised by the material
- C25B11/051—Electrodes formed of electrocatalysts on a substrate or carrier
- C25B11/073—Electrodes formed of electrocatalysts on a substrate or carrier characterised by the electrocatalyst material
- C25B11/091—Electrodes formed of electrocatalysts on a substrate or carrier characterised by the electrocatalyst material consisting of at least one catalytic element and at least one catalytic compound; consisting of two or more catalytic elements or catalytic compounds
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- C25B3/00—Electrolytic production of organic compounds
- C25B3/01—Products
- C25B3/07—Oxygen containing compounds
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- 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
- C25B3/00—Electrolytic production of organic compounds
- C25B3/20—Processes
- C25B3/25—Reduction
- C25B3/26—Reduction of carbon dioxide
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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Abstract
The invention provides a Zn doped Bi 2 O 3 A preparation method of a bimetallic catalyst belongs to the field of new energy nano materials and the technical field of catalysis, and is mainly applied to electrochemical catalysis of carbon dioxide. The main steps of the technical scheme are that dimethyl imidazole is dissolved in methanol, stirred evenly and marked as solution A; zinc nitrate hexahydrate and bismuth nitrate pentahydrateDissolving in methanol, stirring uniformly, and marking as solution B; slowly pouring the solution B into the solution A, continuously stirring uniformly, standing, separating solid from liquid of a reaction product, and drying in a drying oven to obtain a white product; then annealing the white product obtained in the second step in a muffle furnace to obtain Zn doped Bi 2 O 3 Bimetallic catalysts. The Zn doped Bi obtained by the invention 2 O 3 The bimetallic catalyst has excellent catalytic performance in the aspect of carbon dioxide electrocatalysis.
Description
Technical Field
The invention belongs to the field of new energy nano materials and the technical field of catalysis, and in particular relates to a Zn doped Bi 2 O 3 A preparation method of a bimetallic catalyst.
Background
The disclosure of this background section is only intended to increase the understanding of the general background of the invention and is not necessarily to be construed as an admission or any form of suggestion that this information forms the prior art already known to those of ordinary skill in the art.
In recent years, the massive consumption of fossil fuels has led to excessive emissions of greenhouse gases, in particular carbon dioxide (CO) 2 ) And thus cause global problems such as resource exhaustion and a series of extreme weather. So CO is converted into 2 As a potential carbon resource, synthesis of chemical products by various methods has become a consensus. In which the use of electrochemical catalytic reduction is currently the ideal CO 2 Catalytic conversion method can realize CO 2 Directly converts into various energy materials, thereby realizing artificial closed carbon circulation. However, many challenges remain in real-world operation and large-scale industrial applications, such as excessive catalyst cost, poor product selectivity and long-term stability.
Paper Zn doped two-dimensional layered delta-Bi 2 O 3 The research on the photocatalytic nitrogen fixation performance of the nano-sheet discloses that the photo-generated current carrying can be effectively inhibited by doping a modified catalyst to form a trapAnd (3) compounding the particles to obtain high-efficiency photocatalysis nitrogen fixation efficiency. However, there is no concern about the problem of "low cost, high selectivity catalytic electrochemical reduction of carbon dioxide".
Patent CN115304099a discloses surface electronically localized bismuth oxide nanoplatelets and their use in electrocatalytic carbon dioxide reduction and zinc-carbon dioxide cells, but studies have found that: bi-based catalysts have the problems of complicated preparation, poor intrinsic activity, low product selectivity and the like.
Currently, no catalyst has been found in the industry for electrochemical reduction of carbon dioxide with low cost, high selectivity catalysis among a wide variety of catalysts.
Disclosure of Invention
In order to solve the problems, the invention provides a method for preparing Zn-doped Bi with high-efficiency electrochemical reduction of carbon dioxide with low cost and simple manufacture 2 O 3 The bimetallic catalyst solves the problems of complicated preparation, poor intrinsic activity, low product selectivity and the like of the existing Bi-based catalyst.
In order to achieve the above purpose, the present invention adopts the following technical scheme:
in a first aspect of the present invention, there is provided a Zn-doped Bi 2 O 3 A method of preparing a bimetallic catalyst comprising:
dissolving zinc salt and bismuth salt in a solvent to obtain a salt solution;
mixing the salt solution with an alcohol solution of dimethyl imidazole, reacting, and collecting a solid product;
drying and annealing the solid product to obtain Zn doped Bi 2 O 3 A bimetallic catalyst;
wherein the molar ratio of the zinc salt to the bismuth salt is 1-1.5: 1 to 1.5.
In a second aspect of the present invention, there is provided Zn-doped Bi prepared by the above method 2 O 3 Bimetallic catalysts.
In a third aspect of the present invention, there is provided the above Zn-doped Bi 2 O 3 Use of a bimetallic catalyst for catalyzing the electroreduction of carbon dioxide to formic acid and carbon monoxide.
The beneficial effects of the invention are that
(1) The method for preparing Zn doped Bi by adopting the invention 2 O 3 The method of the bimetallic catalyst has the advantages of simple preparation process, low cost and excellent catalytic performance in electrochemical reduction of carbon dioxide. The Zn-Bi interface is presented on a microscopic scale, and the CO can be effectively promoted by the bimetal synergistic effect between Zn-Bi 2 Adsorption on the catalyst surface and reduces the energy barrier for the catalytic reaction.
(2) Zn doped Bi prepared by the invention 2 O 3 The bimetallic catalyst is applied to electrocatalytic carbon dioxide reduction reaction, and effectively inhibits hydrogen evolution reaction. at-1.0V vs. RHE, 108mA cm can be achieved -2 While the faraday efficiencies of formic acid and carbon monoxide can reach 91% and 6%, respectively. The invention can provide thought for designing other bimetallic catalysts for electrochemical reduction of carbon dioxide.
(3) The preparation method is simple, has strong practicability and is easy to popularize.
Drawings
The accompanying drawings, which are included to provide a further understanding of the invention and are incorporated in and constitute a part of this specification, illustrate embodiments of the invention and together with the description serve to explain the invention.
FIG. 1 Zn-doped Bi according to the present invention 2 O 3 A preparation flow chart of the bimetallic catalyst;
FIG. 2 Zn-doped Bi prepared in example 2 of the present invention 2 O 3 Scanning electron microscopy of bimetallic catalysts;
FIG. 3 Zn-doped Bi prepared in example 2 of the present invention 2 O 3 Transmission electron microscopy of bimetallic catalysts;
FIG. 4 Zn-doped Bi prepared in example 2 of the present invention 2 O 3 Transmission electron microscope X-ray energy spectrum of bimetallic catalyst;
FIG. 5 Zn-doped Bi prepared in example 2 of the present invention 2 O 3 Bimetallic catalyst in CO 2 Catalytic performance diagram in electroreduction.
FIG. 6 Zn-doped Bi prepared in example 2 of the present invention 2 O 3 Co of bimetallic catalysts at-1.0V vs. RHE voltage 2 Electroreduction stability test pattern.
Detailed Description
It should be noted that the following detailed description is exemplary and is intended to provide further explanation of the invention. Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs.
Zn doped Bi 2 O 3 A method of preparing a bimetallic catalyst comprising:
step 1, dissolving dimethyl imidazole in methanol, uniformly stirring, and marking as a solution A;
step 2, dissolving zinc nitrate hexahydrate and bismuth nitrate pentahydrate in methanol, uniformly stirring, and marking as a solution B;
step 3, slowly pouring the solution B into the solution A, continuously stirring uniformly, standing, separating solid and liquid of a reaction product, and drying in a drying oven to obtain a white product;
step 4, annealing the white product obtained in the step two in a muffle furnace to obtain Zn doped Bi 2 O 3 Bimetallic catalysts.
In some embodiments, the concentration of the alcoholic solution of dimethylimidazole is between 0.2 and 0.4mmol/ml.
In some embodiments, the zinc salt is zinc nitrate hexahydrate.
In some embodiments, the concentration of zinc salt in the salt solution is from 0.2 to 0.4mmol/ml.
In some embodiments, the bismuth salt is bismuth nitrate pentahydrate.
In some embodiments, the concentration of bismuth salt in the salt solution is 0.2 to 0.4mmol/ml.
In some embodiments, the molar mass ratio of bismuth salt to dimethylimidazole is 1:3-5.
In some embodiments, the annealing temperature is 200-240 ℃ and the annealing time is 2.5-3 hours;
in some embodiments, the rate of temperature increase is 2 to 5 ℃/min.
In some embodiments, the electrode includes, but is not limited to, carbon paper, carbon cloth.
The invention will now be described in further detail with reference to the following specific examples, which should be construed as illustrative rather than limiting.
EXAMPLE 1 Zn-doped Bi 2 O 3 Preparation of bimetallic catalysts
Step 1, 10mmol of dimethyl imidazole is dissolved in 50ml of methanol, stirred for 0.5h and marked as solution A;
step 2,2.5mmol of zinc nitrate hexahydrate and 2.5mmol of bismuth nitrate pentahydrate are dissolved in 50ml of methanol and stirred for 1h and marked as solution B;
step 3, slowly pouring the solution B into the solution A, continuously stirring for 2 hours, standing for 6 hours, separating solid and liquid of a reaction product by a centrifuge at 6000 rpm, and drying for 6 hours at 80 ℃ in a drying box to obtain a white product;
step 4, annealing the white product obtained in the step two in a muffle furnace at 200 ℃ for 3 hours, wherein the heating rate is 5 ℃/min, and finally obtaining the Zn doped Bi 2 O 3 Bimetallic catalysts.
EXAMPLE 2 Zn-doped Bi 2 O 3 Preparation of bimetallic catalysts
Step 1, 16mmol of dimethyl imidazole is dissolved in 50ml of methanol, stirred for 0.5h and marked as solution A;
step 2,4mmol of zinc nitrate hexahydrate and 4mmol of bismuth nitrate pentahydrate are dissolved in 50ml of methanol, stirred for 1h and marked as solution B;
step 3, slowly pouring the solution B into the solution A, continuously stirring for 2 hours, standing for 6 hours, separating solid and liquid of a reaction product by a centrifuge at 6000 rpm, and drying for 6 hours at 80 ℃ in a drying box to obtain a white product;
step 4, annealing the white product obtained in the step two in a muffle furnace at 200 ℃ for 3 hours, wherein the heating rate is 5 ℃/min, and finally obtaining the Zn doped Bi 2 O 3 Bimetallic catalysts.
EXAMPLE 3 Zn-doped Bi 2 O 3 Preparation of bimetallic catalysts
Step 1, dissolving 20mmol of dimethyl imidazole in 50ml of methanol, stirring for 0.5h, and marking as a solution A;
step 2,5mmol of zinc nitrate hexahydrate and 5mmol of bismuth nitrate pentahydrate are dissolved in 50ml of methanol, stirred for 1h and marked as solution B;
step 3, slowly pouring the solution B into the solution A, continuously stirring for 2 hours, standing for 6 hours, separating solid and liquid of a reaction product by a centrifuge at 6000 rpm, and drying for 6 hours at 80 ℃ in a drying box to obtain a white product;
step 4, annealing the white product obtained in the step two in a muffle furnace at 200 ℃ for 3 hours, wherein the heating rate is 5 ℃/min, and finally obtaining the Zn doped Bi 2 O 3 Bimetallic catalysts.
EXAMPLE 4 Zn-doped Bi 2 O 3 Preparation of bimetallic catalysts
Step 1, dissolving 20mmol of dimethyl imidazole in 50ml of methanol, stirring for 0.5h, and marking as a solution A;
step 2,5mmol of zinc nitrate hexahydrate and 5mmol of bismuth nitrate pentahydrate are dissolved in 50ml of methanol, stirred for 1h and marked as solution B;
step 3, slowly pouring the solution B into the solution A, continuously stirring for 2 hours, standing for 6 hours, separating solid and liquid of a reaction product by a centrifuge at 6000 rpm, and drying for 6 hours at 80 ℃ in a drying box to obtain a white product;
step 4, annealing the white product obtained in the step two in a muffle furnace at 200 ℃ for 3 hours, wherein the heating rate is 2 ℃/min, and finally obtaining the Zn doped Bi 2 O 3 Bimetallic catalysts.
EXAMPLE 5 Zn-doped Bi 2 O 3 Electrode preparation of bimetallic catalysts
10mg of the catalyst prepared in example 1 was uniformly dispersed in a mixed solution of 50ml of naphthol and 950ml of absolute ethanol, and then a certain amount of the mixed solution was uniformly coated on an electrode (carbon cloth) and was used after natural drying.
Examples6Zn doped Bi 2 O 3 Electrode preparation of bimetallic catalysts
20mg of the catalyst prepared in example 1 was uniformly dispersed in a mixed solution of 100ml of naphthol and 900ml of absolute ethanol, and then a certain amount of the mixed solution was uniformly coated on an electrode (carbon cloth) and was used after natural drying.
EXAMPLE 7 Zn-doped Bi 2 O 3 Bimetallic catalyst in CO 2 Application to electrochemical reduction
The electrochemical test of this example was performed in a flow cell. The gas diffusion electrodes prepared in examples 5 and 6 were used as working electrodes, platinum sheets as counter electrodes, and Ag/AgCl as reference electrode, respectively. Controlling CO using mass flow meter 2 The flow rate of (2) is 20ml/min; the electrolyte is 1M KOH solution; using an electrochemical workstation to measure the system; the gas and liquid phase products were quantitatively analyzed by gas chromatography and nuclear magnetism, respectively.
As shown in FIG. 5, the present invention can achieve-108 mA cm at-1.0V vs. RHE -2 While the faraday efficiencies of formic acid and carbon monoxide can reach 91% and 6%, respectively.
As shown in FIG. 6, the electrode prepared by the invention always maintains high catalytic efficiency in the continuous electroreduction process for up to 12 hours, and has better stability.
The above description is only of the preferred embodiments of the present invention and is not intended to limit the present invention, but various modifications and variations can be made to the present invention by those skilled in the art. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present invention should be included in the protection scope of the present invention.
Claims (10)
1. Zn doped Bi 2 O 3 A method for preparing a bimetallic catalyst, comprising:
dissolving zinc salt and bismuth salt in a solvent to obtain a salt solution;
mixing the salt solution with an alcohol solution of dimethyl imidazole, reacting, and collecting a solid product;
drying and annealing the solid product to obtain Zn doped Bi 2 O 3 A bimetallic catalyst;
wherein the molar ratio of the zinc salt to the bismuth salt is 1-1.5: 1 to 1.5.
2. Zn-doped Bi according to claim 1 2 O 3 The preparation method of the bimetallic catalyst is characterized in that the concentration of the alcohol solution of the dimethyl imidazole is 0.2-0.4 mmol/ml.
3. Zn-doped Bi according to claim 1 2 O 3 The preparation method of the bimetallic catalyst is characterized in that the zinc salt is zinc nitrate hexahydrate.
4. Zn-doped Bi according to claim 1 2 O 3 The preparation method of the bimetallic catalyst is characterized in that the concentration of zinc salt in the salt solution is 0.2-0.4 mmol/ml.
5. Zn-doped Bi according to claim 1 2 O 3 The preparation method of the bimetallic catalyst is characterized in that the bismuth salt is bismuth nitrate pentahydrate.
6. Zn-doped Bi according to claim 1 2 O 3 The preparation method of the bimetallic catalyst is characterized in that the concentration of bismuth salt in the salt solution is 0.2-0.4 mmol/ml.
7. Zn-doped Bi according to claim 1 2 O 3 The preparation method of the bimetallic catalyst is characterized in that the molar mass ratio of bismuth salt to dimethyl imidazole is 1:3-5.
8. Zn-doped Bi according to claim 1 2 O 3 The preparation method of the bimetallic catalyst is characterized in that the annealing temperature is 200-240 ℃ and the annealing time is 2.5-3 h;
or the temperature rising rate is 2-5 ℃/min.
9. Zn-doped Bi prepared by the method of any one of claims 1 to 8 2 O 3 Bimetallic catalysts.
10. The Zn-doped Bi of claim 9 2 O 3 Use of a bimetallic catalyst for catalyzing the electroreduction of carbon dioxide to formic acid and carbon monoxide.
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