CN115896810B - Noble metal monoatomic catalyst based on high entropy effect and preparation method thereof - Google Patents

Noble metal monoatomic catalyst based on high entropy effect and preparation method thereof Download PDF

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CN115896810B
CN115896810B CN202211479510.2A CN202211479510A CN115896810B CN 115896810 B CN115896810 B CN 115896810B CN 202211479510 A CN202211479510 A CN 202211479510A CN 115896810 B CN115896810 B CN 115896810B
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CN115896810A (en
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许海涛
边筱扉
邱华军
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Dongguan University of Technology
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Abstract

The invention relates to the technical field of electrochemical catalysis, in particular to a noble metal monoatomic catalyst based on a high entropy effect and a preparation method thereof, wherein the noble metal monoatomic catalyst is a noble metal monoatomic supported high entropy oxyhydroxide catalyst, and the molecular formula of the high entropy oxyhydroxide is Zn 3‑x V 2 M x (OH) 2 O 7 ·2H 2 O, wherein M is an optional metal and is three or more of Ni, co, fe, cu, al, mn, and the noble metal monoatomic species is one or more of Au, ru, in, pt. The noble metal single-atom composite catalyst prepared by the method has regular appearance, good crystallinity and adjustable metal element types and proportions of the high-entropy hydroxyl oxide substrate, can be used for preparing various noble metal single-atom catalysts, and has wide application prospects in the field of catalysis.

Description

Noble metal monoatomic catalyst based on high entropy effect and preparation method thereof
Technical Field
The invention relates to the technical field of electrochemical catalysis, in particular to a noble metal monoatomic catalyst based on a high entropy effect and a preparation method thereof.
Background
The energy is a basic stone for existence and development of human society, is a basic constraint condition for economic development and civilization progress, and is an important foundation for national economy and national security and sustainable development. Under the guidance of 'carbon peak, carbon neutralization', following the rapid development of new energy sources such as solar energy, wind energy and the like, hydrogen energy is coming out as a recognized zero-carbon energy source. The preparation technology of hydrogen mainly comprises fossil fuel hydrogen production, electrolytic water hydrogen production, photolytic water hydrogen production and biological hydrogen production.
The hydrogen production process by water electrolysis is simple, the product purity is high, and the high-efficiency, clean and large-scale preparation of hydrogen can be realized by adopting renewable energy sources as energy sources. However, electrolyzed water is a complex redox reaction process involving multiple electron transfer from the anode to the cathode, and thus the electrolyzed water catalyst is one of the key factors determining the cost of hydrogen production by electrolysis of water.
The most widely used in industry is alkaline water electrolysis technology at present, and under the current technical conditions, noble metal platinum and yttrium oxide/ruthenium oxide are respectively cathode and anode catalysts with higher catalytic efficiency, but the industrial application of the noble metal platinum and the yttrium oxide/ruthenium oxide is severely limited by the expensive price and poor stability of the noble metal platinum and the yttrium oxide/ruthenium oxide. Therefore, the water electrolysis catalyst for improving the utilization rate and the catalytic stability of the noble metal catalyst is a key for large-scale popularization of the core competitiveness of the technology.
The high-entropy hydroxyl oxide is a novel functional material which is derived and developed on the basis of high-entropy alloy and consists of oxygen ions, hydroxyl ions and five or more metal elements and has unique structure and function adjustable characteristics. In highly disordered multicomponent systems, high entropy oxyhydroxide produces a unique set of properties such as lattice distortion effects, high entropy effects, delayed diffusion effects, and cocktail effects due to the large mixing entropy.
In recent years, a single-atom composite material is used as a novel catalyst, and the noble metal atoms are anchored on a substrate, so that the atom utilization rate and stability of the noble metal can be greatly improved, and the single-atom composite material has a unique electronic structure and excellent catalytic performance and is becoming a research hot spot in the catalytic field. However, noble metal monoatoms have very high surface free energy, making them susceptible to agglomeration to form clusters and nanoparticles, and therefore the preparation of monoatomic catalysts is a challenge; meanwhile, on the other hand, the larger doping amount is easy to agglomerate to form clusters, but too low doping amount cannot ensure the number of the catalytic active sites, so that the activity of the single-atom catalyst is influenced to a certain extent. Therefore, the preparation method of the noble metal monoatomic catalyst with uniform scale and rich catalytic active sites is still in a research and development stage.
Disclosure of Invention
The invention provides a noble metal monoatomic catalyst based on a high entropy effect and a preparation method thereof, which can overcome the problems of low loading capacity and uneven fraction of the monoatomic catalyst in the prior art.
A noble metal monoatomic catalyst based on high entropy effect is a noble metal monoatomic supported high entropy hydroxyl oxide catalyst, and the molecular formula of the high entropy hydroxyl oxide is Zn 3-x V 2 M x (OH) 2 O 7 ·2H 2 O, wherein M is an optional metal and is three or more of Ni, co, fe, cu, al, mn, and the noble metal monoatomic species is one or more of Au, ru, in, pt.
Preferably, the atomic percentage of each optional metal element to all non-noble metal elements is 0.05-0.3.
The preparation method of the noble metal monoatomic catalyst based on the high entropy effect specifically comprises the following steps:
s1, adding vanadium pentoxide and inorganic non-noble metal salt into distilled water serving as a solvent, and carrying out ultrasonic mixing to obtain a mixed metal salt solution;
step S2, under the magnetic stirring condition, sequentially adding a mixed metal salt solution, noble metal monoatomic metal salt, urotropine and anhydrous sodium sulfate, and fully and uniformly mixing to obtain a precursor solution;
and S3, transferring the precursor solution in the step S2 into a reaction kettle for hydrothermal reaction, cooling, collecting gray brown powder on the upper layer in the reaction kettle, centrifugally washing, and vacuum drying to obtain the noble metal monoatomic catalyst.
Preferably, the inorganic non-noble metal salt in step S1 is a nitrate, sulfate and/or hydrochloride.
Preferably, the noble metal monoatomic metal salt in step S2 is chloroauric acid, ruthenium chloride, chloroplatinic acid, indium chloride/indium nitrate/indium sulfate.
Preferably, the ultrasonic treatment time of the mixed metal salt solution in step S1 is 30-60min.
Preferably, the reaction temperature of the hydrothermal reaction in the step S3 is 110-130 ℃ and the reaction time is 24-36h.
Preferably, the concentration of vanadium ions in the precursor solution in step S2 is 0.14 to 0.17 mol.L -1 The concentration of zinc ions is 0.03-0.05mol.L -1 Sodium sulfate of 0.10-0.14 mol.L -1 The urotropine concentration is 0.06-0.11 mol.L -1 The concentration of the inorganic non-noble metal salt is 0.01-0.02 mol.L -1 The concentration of the noble metal monoatomic metal salt is 0.001-0.005 mol.L -1
The invention has the remarkable technical effects due to the adoption of the technical scheme:
(1) The noble metal monoatomic catalyst is a noble metal monoatomic supported high-entropy hydroxyl oxide catalyst, the substrate of the noble metal monoatomic catalyst is high-entropy hydroxyl oxide, and the noble metal monoatomic catalyst is an excellent electrolyzed water catalyst based on the unique property of the high-entropy hydroxyl oxide, so that the activity of the catalyst can be improved to a certain extent, and meanwhile, the noble metal monoatomic catalyst can be used as an excellent carrier to anchor noble metal monoatomic and improve the loading capacity and stability of the monoatomic.
(2) The high-entropy hydroxyl oxide of the substrate has good crystallinity, regular morphology and adjustable metal element types and proportion, and the cocktail effect of the high-entropy compound can also change the coordination environment of the single-atom catalyst, further regulate and control the electronic structure of the noble metal single-atom catalyst, optimize the coordination environment of the catalyst and further prepare the single-atom catalyst with multifunctional catalytic property.
(3) The types and the proportions of the metal elements in the high-entropy hydroxyl oxides are adjustable, and the special high-entropy effect can provide coordination environment and bonding effect for anchoring different types of noble metal monoatoms. Therefore, the invention provides a general single-atom catalyst synthesis strategy, and provides a new idea for controllable preparation of the single-atom catalyst.
Drawings
FIG. 1 is a scanning electron microscope image of zinc vanadium aluminum nickel cobalt iron copper manganese oxyhydroxide supported by monoatomic ruthenium Jin Boyin prepared in example 1;
FIG. 2 is an X-ray powder diffraction pattern of the monoatomic ruthenium Jin Boyin loaded zinc vanadium aluminum nickel cobalt iron copper manganese oxyhydroxide prepared in example 1;
FIG. 3 is an X-ray energy spectrum of a single-atom ruthenium Jin Boyin loaded zinc vanadium aluminum nickel cobalt iron copper manganese oxyhydroxide prepared in example 1;
FIG. 4 is a high angle annular dark field transmission and energy spectrum plot of the monoatomic ruthenium Jin Boyin loaded zinc vanadium aluminum nickel cobalt iron copper manganese oxyhydroxide prepared in example 1;
FIG. 5 is a spherical aberration correcting transmission electron microscope image of zinc vanadium aluminum nickel cobalt iron copper manganese oxyhydroxide supported by monoatomic ruthenium Jin Boyin prepared in example 1;
FIG. 6 is an electrolyzed water polarization curve of a monoatomic ruthenium Jin Boyin loaded zinc vanadium aluminum nickel cobalt iron copper manganese oxyhydroxide working electrode prepared in example 1;
FIG. 7 is an X-ray powder diffraction pattern of zinc vanadium aluminum nickel cobalt iron oxyhydroxide loaded with ruthenium indium monoatomate prepared in example 2;
FIG. 8 is a spherical aberration correcting transmission electron microscope image of single atom platinum supported zinc vanadium aluminum nickel cobalt iron oxyhydroxide prepared in example 2;
FIG. 9 is an X-ray powder diffraction pattern of a single-atom platinum-supported zinc-vanadium-nickel-copper-manganese oxyhydroxide prepared in example 3;
FIG. 10 is a spherical aberration correcting transmission electron microscope image of single atom platinum supported zinc vanadium nickel copper manganese oxyhydroxide prepared in example 3.
Detailed Description
For a further understanding of the present invention, the present invention will be described in detail with reference to the drawings and examples. It is to be understood that the examples are illustrative of the present invention and are not intended to be limiting.
Example 1
The embodiment 1 of the invention relates to a noble metal monoatomic catalyst based on a high entropy stabilization effect, in particular to a zinc vanadium aluminum nickel cobalt iron copper manganese oxyhydroxide catalyst loaded by monoatomic ruthenium Jin Boyin, and the preparation method comprises the following steps:
(1) Adding a proper amount of distilled water as a solvent into a container, sequentially adding reagents of vanadium pentoxide, zinc nitrate, aluminum nitrate, nickel nitrate, cobalt nitrate, ferric nitrate, copper nitrate and manganese nitrate, and controlling the concentration of vanadium ions in the solution to be 0.14 mol.L -1 The concentration of zinc ions is 0.03 mol.L -1 The concentration of aluminum ions is 0.01 mol.L -1 The concentration of nickel ions is 0.01 mol.L -1 Cobalt ion concentration of 0.01 mol.L -1 Iron ion concentration of 0.01 mol.L -1 Copper ion concentration of 0.01 mol.L -1 The concentration of manganese ions is 0.01 mol.L -1 Carrying out ultrasonic treatment on the mixed solution for 30 minutes to ensure that the solution is uniformly mixed;
(2) Sequentially adding the mixed solution, chloroauric acid, ruthenium chloride, indium nitrate, chloroplatinic acid, urotropine and sodium sulfate reagent in the step (1) on the basis of magnetic stirring, wherein the adding time interval of each reagent is 5 minutes, the magnetic stirring is carried out for 30 minutes after the mixing is completed, and the concentration of gold ions in the precursor solution is controlled to be 0.001 mol.L -1 Ruthenium ion concentration of 0.001 mol.L -1 The concentration of indium ions is 0.001 mol.L -1 Platinum ion concentration of 0.001 mol.L -1 The urotropine concentration is 0.06 mol.L -1 The concentration of sodium sulfate is 0.10 mol.L -1 Finally, carrying out ultrasonic treatment on the mixed solution stirred by magnetic force for 60 minutes to ensure that the solution is uniformly mixed;
(3) Transferring the mixed solution obtained in the step (2) into a reaction kettle, sealing the reaction kettle, performing hydrothermal reaction at 110 ℃ for 24 hours, cooling, collecting gray brown powder on the upper layer in the reaction kettle, centrifugally washing, and drying to obtain the zinc-vanadium-aluminum-nickel-cobalt-iron-copper-manganese oxyhydroxide loaded by monoatomic ruthenium Jin Boyin.
Referring to the drawings, fig. 1 is a scanning electron microscope image of zinc-vanadium-aluminum-nickel-cobalt-iron-copper-manganese oxyhydroxide loaded by monoatomic ruthenium Jin Boyin prepared in the embodiment, and the image shows that the monoatomic catalyst prepared in the embodiment is of a nano-sheet structure and regular in morphology, and no obvious attachments such as nano particles exist on the surface of the nano-sheet.
Fig. 2 and 3 are respectively an X-ray powder diffraction pattern and an X-ray energy spectrum of zinc-vanadium-aluminum-nickel-cobalt-iron-copper-manganese oxyhydroxide loaded by monoatomic ruthenium Jin Boyin prepared in this example, all diffraction peaks in the X-ray powder diffraction pattern have obvious left shift relative to standard card JCPDF no#50-0750, and diffraction peaks of other impurities are absent, and the X-ray energy spectrum proves that the prepared catalyst contains zinc, vanadium, aluminum, nickel, cobalt, iron, copper, manganese, ruthenium, gold, platinum and indium metal elements. At the same time, the combination of ICP test can prove that the noble metal monoatomic catalyst synthesized by the example is RuAuPtIn@Zn 2.7 V 2 Al 0.05 Ni 0.05 Co 0.05 Fe 0.05 Cu 0.05 Mn 0.05 (OH) 2 O 7 ·2H 2 O。
Fig. 4 is a high-angle annular dark field diagram and energy spectrum surface scanning diagram of zinc-vanadium-aluminum-nickel-cobalt-iron-copper-manganese oxyhydroxide loaded by monoatomic ruthenium Jin Boyin prepared in the embodiment, wherein all metal elements on the data surface are uniformly distributed on the nanosheets, and obvious element aggregation and enrichment do not occur.
FIG. 5 is a spherical aberration correction transmission electron microscope image of a single-atom ruthenium Jin Boyin loaded zinc-vanadium-aluminum-nickel-cobalt-iron-copper-manganese oxyhydroxide, wherein heavy metal elements ruthenium, gold, platinum and indium on the surface of data are dispersed on a zinc-vanadium-aluminum-nickel-cobalt-iron-copper-manganese high-entropy oxyhydroxide nano-sheet in a single-atom mode.
Therefore, from fig. 1, fig. 2, fig. 3, fig. 4 and fig. 5, we can see that we successfully prepare the zinc vanadium aluminum nickel cobalt iron copper manganese oxyhydroxide nano-sheet material loaded by the monoatomic ruthenium Jin Boyin.
The prepared high-entropy hydroxyl oxide is manufactured into an oxygen evolution reaction working electrode, the polarization curve test result is shown in fig. 5, and the catalytic activity of the crystalline porous high-entropy zinc vanadium aluminum nickel cobalt iron ruthenium hydroxyl oxide catalyst product is greatly improved compared with that of commercial ruthenium oxide as shown in fig. 5, because the prepared high-entropy hydroxyl oxide has higher specific surface area and rich catalytic active sites, and the electronic structure of the catalyst can be regulated and controlled by the cocktail effect of the high-entropy compound, and finally the activity of the catalyst is improved.
Example 2
The procedure of example 1 was followed except that the zinc vanadium aluminum nickel cobalt iron oxyhydroxide catalyst material loaded with ruthenium indium monoatomate was prepared according to the following procedure:
(1) Adding proper distilled water as solvent into a container, sequentially adding reagents of vanadium pentoxide, zinc sulfate, aluminum sulfate, nickel sulfate, cobalt sulfate and ferric sulfate, and controlling the concentration of vanadium ions in the solution to be 0.17 mol.L -1 The concentration of zinc ions is 0.05 mol.L -1 The concentration of aluminum ions is 0.02 mol.L -1 The concentration of nickel ions is 0.02 mol.L -1 Cobalt ion concentration of 0.02 mol.L -1 The concentration of iron ions is 0.02 mol.L -1 Carrying out ultrasonic treatment on the mixed solution for 60 minutes to ensure that the solution is uniformly mixed;
(2) Sequentially adding the mixed solution, ruthenium chloride, indium chloride, urotropine and sodium sulfate in the step (1) on the basis of magnetic stirring, wherein the adding time of each reagent is 5 minutes, the magnetic stirring is carried out for 30 minutes after the mixing is finished, and the concentration of ruthenium ions in the precursor solution is controlled to be 0.005 mol.L -1 The concentration of indium ions is 0.005 mol.L -1 The urotropine concentration is 0.11 mol.L -1 The concentration of sodium sulfate is 0.14 mol.L -1 Finally, carrying out ultrasonic treatment on the mixed solution stirred by magnetic force for 60 minutes to ensure that the solution is uniformly mixed;
(3) Transferring the mixed solution obtained in the step (2) into a reaction kettle, sealing the reaction kettle, performing hydrothermal reaction at 130 ℃ for 36 hours, cooling, collecting gray brown powder on the upper layer in the reaction kettle, centrifugally washing, and drying to obtain the product, namely the zinc-vanadium-aluminum-nickel-cobalt-iron oxyhydroxide loaded by monoatomic ruthenium-indium.
Referring to the drawings, FIGS. 7 and 8 are respectively an X-ray powder diffraction pattern and a spherical aberration correction transmission electron microscope image of zinc-vanadium-aluminum-nickel-cobalt-iron oxyhydroxide loaded with single-atom ruthenium-indium, prepared in this example, all diffraction peaks in the X-ray powder diffraction patternThere was a significant left shift relative to the standard card JCPDF NO #50-0750 and NO diffraction peaks of other impurities. Meanwhile, the noble metal monoatomic catalyst synthesized by the example can be proved to be RuIn@Zn by combining ICP test and spherical aberration correction transmission electron microscope 1.8 V 2 Al 0.3 Ni 0.3 Co 0.3 Fe 0.3 (OH) 2 O 7 ·2H 2 O。
Example 3
The procedure of example 1 was followed except that the single-atom platinum-supported zinc vanadium aluminum nickel copper manganese oxyhydroxide catalyst material was prepared as follows:
(1) Adding proper distilled water as solvent into a container, sequentially adding vanadium pentoxide, zinc chloride, ferric sulfate, cupric chloride and manganese sulfate, and controlling the concentration of vanadium ion in the solution to be 0.15 mol.L -1 The concentration of zinc ions is 0.04 mol.L -1 The concentration of aluminum ions is 0.018 mol.L -1 The concentration of nickel ions is 0.018 mol.L -1 Copper ion concentration of 0.018 mol.L -1 The concentration of manganese ions is 0.018 mol.L -1 Carrying out ultrasonic treatment on the mixed solution for 40 minutes to ensure that the solution is uniformly mixed;
(2) Sequentially adding the mixed solution, chloroplatinic acid, urotropine and sodium sulfate reagent in the step (1) on the basis of magnetic stirring, wherein the adding time of each reagent is 5 minutes, the magnetic stirring is carried out for 30 minutes after the mixing is finished, and the concentration of platinum ions in the precursor solution is controlled to be 0.004 mol.L -1 The urotropine concentration is 0.1 mol.L -1 The concentration of sodium sulfate is 0.13 mol.L -1 Finally, carrying out ultrasonic treatment on the mixed solution stirred by magnetic force for 60 minutes to ensure that the solution is uniformly mixed;
(3) Transferring the mixed solution obtained in the step (2) into a reaction kettle, sealing the reaction kettle, performing hydrothermal reaction at 120 ℃ for 30 hours, cooling, collecting gray brown powder on the upper layer in the reaction kettle, centrifugally washing, and drying to obtain the product, namely the zinc-vanadium-aluminum-nickel-copper-manganese oxyhydroxide loaded by single-atom platinum.
Referring to the drawings, FIGS. 9 and 10 are X-ray powders of single-atom platinum-supported zinc-vanadium-nickel-iron-manganese oxyhydroxide prepared in the present exampleThe diffraction pattern and the spherical aberration correction transmission electron microscope pattern have all diffraction peaks in the X-ray powder diffraction pattern significantly shifted to the left relative to the standard card JCDF NO#50-0750, and have NO diffraction peaks of other impurities. Meanwhile, the noble metal monoatomic catalyst synthesized by the example can be proved to be Pt@Zn by combining ICP test and spherical aberration correction transmission electron microscope image 2.24 V 2 Al 0.19 Ni 0.19 Cu 0.19 Mn 0.19 (OH) 2 O 7 ·2H 2 O。
Example 4
The procedure of example 1 is followed except that in this example, a single atom indium platinum supported zinc vanadium iron copper manganese oxyhydroxide catalyst material is prepared as follows:
(1) Adding proper distilled water as solvent into a container, sequentially adding vanadium pentoxide, zinc chloride, ferric chloride, cupric chloride and manganese chloride reagent, and controlling the concentration of vanadium ion in the solution to be 0.15 mol.L -1 The concentration of zinc ions is 0.04 mol.L -1 Cobalt ion concentration of 0.015 mol.L -1 The concentration of iron ions is 0.015 mol.L -1 Copper ion concentration of 0.015 mol.L -1 The concentration of manganese ions is 0.015 mol.L -1 Carrying out ultrasonic treatment on the mixed solution for 40 minutes to ensure that the solution is uniformly mixed;
(2) Sequentially adding the mixed solution, indium sulfate, chloroplatinic acid, urotropine and sodium sulfate in the step (1) on the basis of magnetic stirring, wherein the adding time of each reagent is 5 minutes, the magnetic stirring is carried out for 30 minutes after the mixing is finished, and the concentration of indium ions in the precursor solution is controlled to be 0.003 mol.L -1 Platinum ion concentration of 0.003 mol.L -1 The urotropine concentration is 0.09 mol.L -1 The concentration of sodium sulfate is 0.12 mol.L -1 Finally, carrying out ultrasonic treatment on the mixed solution stirred by magnetic force for 60 minutes to ensure that the solution is uniformly mixed;
(3) Transferring the mixed solution obtained in the step (2) into a reaction kettle, sealing the reaction kettle, performing hydrothermal reaction at 120 ℃ for 30 hours, cooling, collecting gray brown powder on the upper layer in the reaction kettle, centrifugally washing, and drying to obtain the product, namely the zinc-vanadium-iron-copper-manganese oxyhydroxide loaded by single-atom indium-platinum. Combined with XRD, ICP measurementTests prove that the noble metal monoatomic catalyst synthesized by the example is InPt@Zn 2.49 V 2 Fe 0.17 Cu 0.17 Mn 0.17 (OH) 2 O 7 ·2H 2 O。
Example 5
The procedure of example 1 is followed except that in this example, a single atom platinum indium supported zinc vanadium aluminum nickel cobalt iron manganese oxyhydroxide catalyst material is prepared as follows:
(1) Adding proper distilled water as solvent into a container, sequentially adding vanadium pentoxide, zinc nitrate, aluminum chloride, nickel nitrate, cobalt chloride, ferric nitrate and manganese sulfate reagent, and controlling the concentration of vanadium ion in the solution to be 0.16mol.L -1 The concentration of zinc ions is 0.04 mol.L -1 The concentration of aluminum ions is 0.013 mol.L -1 The concentration of nickel ions is 0.013 mol.L -1 Cobalt ion concentration of 0.013 mol.L -1 The concentration of iron ions is 0.013mol.L -1 The concentration of manganese ions is 0.013mol.L -1 Carrying out ultrasonic treatment on the mixed solution for 30 minutes to ensure that the solution is uniformly mixed;
(2) Sequentially adding the mixed solution, chloroauric acid, indium sulfate, chloroplatinic acid, urotropine and sodium sulfate reagent in the step (1) on the basis of magnetic stirring, wherein the adding time interval of each reagent is 5 minutes, and the magnetic stirring is carried out for 30 minutes after the mixing is finished, so that the gold ion concentration in the precursor solution is controlled to be 0.002 mol.L -1 The concentration of indium ions is 0.002 mol.L -1 Platinum ion concentration of 0.002 mol.L -1 The urotropine concentration is 0.1 mol.L -1 The concentration of sodium sulfate is 0.12 mol.L -1 Finally, carrying out ultrasonic treatment on the mixed solution stirred by magnetic force for 60 minutes to ensure that the solution is uniformly mixed;
(3) Transferring the mixed solution obtained in the step (2) into a reaction kettle, sealing the reaction kettle, performing hydrothermal reaction at 120 ℃ for 28 hours, cooling, collecting gray brown powder on the upper layer in the reaction kettle, centrifugally washing, and drying to obtain the single-atomic gold platinum-indium loaded zinc-vanadium-aluminum-nickel-cobalt-iron-manganese oxyhydroxide. The combination of XRD and ICP tests can prove that the noble metal monoatomic catalyst synthesized by the example is PtAuIn@Zn 2.25 V 2 Al 0.15 Ni 0.15 Co 0.15 Fe 0.15 Mn 0.15 (OH) 2 O 7 ·2H 2 O。
The invention and its embodiments have been described above by way of illustration and not limitation, and the invention is illustrated in the accompanying drawings and described in the drawings in which the actual structure is not limited thereto. Therefore, if one of ordinary skill in the art is informed by this disclosure, the structural mode and the embodiments similar to the technical scheme are not creatively designed without departing from the gist of the present invention.

Claims (7)

1. A noble metal monoatomic catalyst based on high entropy effect is characterized in that: the catalyst is a noble metal monoatomically supported high-entropy hydroxyl oxide catalyst, and the molecular formula of the high-entropy hydroxyl oxide is Zn 3-x V 2 M x (OH) 2 O 7 ·2H 2 O, wherein M is more than three kinds of Ni, co, fe, cu, al, mn, and noble metal monoatoms are more than one kind of Au, ru, in, pt.
2. A noble metal monoatomic catalyst based on the high entropy effect according to claim 1, characterized in that: each metal element M accounts for 0.05-0.3 atomic percent of all non-noble metal elements.
3. A method for preparing a noble metal monoatomic catalyst based on high entropy effect according to claim 1 or 2, characterized in that it comprises the following steps:
s1, adding vanadium pentoxide and inorganic non-noble metal salt into distilled water serving as a solvent, and ultrasonically mixing to obtain a mixed metal salt solution, wherein the inorganic non-noble metal salt is nitrate, sulfate and/or hydrochloride;
step S2, under the magnetic stirring condition, sequentially adding a mixed metal salt solution, a noble metal monoatomic metal source, urotropine and anhydrous sodium sulfate, and fully and uniformly mixing to obtain a precursor solution;
and S3, transferring the precursor solution in the step S2 into a reaction kettle for hydrothermal reaction, cooling, collecting gray brown powder on the upper layer in the reaction kettle, centrifugally washing, and vacuum drying to obtain the noble metal monoatomic catalyst.
4. A method for preparing a noble metal monoatomic catalyst based on high entropy effect according to claim 3, characterized in that: in the step S2, the noble metal monoatomic metal source is one or more of chloroauric acid, ruthenium chloride, chloroplatinic acid, indium chloride, indium nitrate or indium sulfate.
5. A method for preparing a noble metal monoatomic catalyst based on high entropy effect according to claim 3, characterized in that: the ultrasonic treatment time of the mixed metal salt solution in the step S1 is 30-60min.
6. A method for preparing a noble metal monoatomic catalyst based on high entropy effect according to claim 3, characterized in that: the reaction temperature of the hydrothermal reaction in the step S3 is 110-130 ℃ and the reaction time is 24-36h.
7. A method for preparing a noble metal monoatomic catalyst based on high entropy effect according to claim 3, characterized in that: the concentration of vanadium ions in the precursor solution in the step S2 is 0.14 to 0.17 mol.L -1 The concentration of zinc ions is 0.03-0.05mol.L -1 Sodium sulfate of 0.10-0.14 mol.L -1 The urotropine concentration is 0.06-0.11 mol.L -1 The concentration of the metal M salt is 0.01-0.02 mol.L -1 The concentration of the noble metal monoatomic metal source is 0.001-0.005 mol.L -1
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