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CN110354848B - PtRu catalyst and preparation method and application thereof - Google Patents

PtRu catalyst and preparation method and application thereof Download PDF

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Publication number
CN110354848B
CN110354848B CN201910441507.3A CN201910441507A CN110354848B CN 110354848 B CN110354848 B CN 110354848B CN 201910441507 A CN201910441507 A CN 201910441507A CN 110354848 B CN110354848 B CN 110354848B
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ptru catalyst
ruo
ruthenium
substrate material
precursor
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CN110354848A (en
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杨生春
李璐
王斌
刘博�
余建平
余瀚威
蒋浩特
许国君
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Ozosl Technology Co ltd
Xian Jiaotong University
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Ozosl Technology Co ltd
Xian Jiaotong University
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/40Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
    • B01J23/46Ruthenium, rhodium, osmium or iridium
    • B01J23/462Ruthenium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/30Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
    • B01J35/33Electric or magnetic properties
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00Electrolytic production of inorganic compounds or non-metals
    • C25B1/01Products
    • C25B1/02Hydrogen or oxygen
    • C25B1/04Hydrogen or oxygen by electrolysis of water
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B11/00Electrodes; Manufacture thereof not otherwise provided for
    • C25B11/04Electrodes; Manufacture thereof not otherwise provided for characterised by the material
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/36Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

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  • Chemical Kinetics & Catalysis (AREA)
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Abstract

The invention discloses a preparation method of a PtRu catalyst, which comprises the following steps: s1, soaking the substrate material in ruthenium salt solution to load ruthenium on the substrate material, taking out the substrate material and drying; s2, placing the dried substrate material in a muffle furnace for calcination to obtain RuO2A precursor; s3 comparing RuO obtained in step S22The precursor is placed in a three-electrode electrolytic cell, and the electrolyte is sulfuric acid solution, Pt net, mercuric mercurous sulfate and obtained RuO2Precursors as counter, reference and working electrodes, RuO2The precursor electrodeposits Pt to obtain the PtRu catalyst. The preparation method of the PtRu catalyst disclosed by the invention is simple in synthesis method, and the prepared PtRu catalyst has good catalytic stability in acidic and alkaline electrolytes. The invention also discloses the PtRu catalyst and application thereof as an electrolytic water hydrogen evolution electrode.

Description

PtRu catalyst and preparation method and application thereof
Technical Field
The invention relates to the technical field of materials, in particular to a PtRu catalyst, a preparation method thereof and application thereof as an electrode for hydrogen evolution by water electrolysis.
Background
Due to the increasing severity of energy crisis and the environmental problems caused by traditional fossil energy, the search for new green energy becomes an urgent problem to be solved.
The hydrogen energy has no pollution to the environment due to the higher energy density, and is an ideal alternative energy source. In the process of preparing hydrogen, a method for preparing hydrogen by electrolyzing water is advocated. However, during the electrolysis of water, an excessively high overpotential causes a problem of high energy consumption, reducing energy conversion efficiency. Therefore, the development of a high-efficiency water electrolysis catalyst is of great significance.
At present, Pt-based catalysts remain ideal catalysts for electrolytic water reactions. However, the metal Pt is relatively deficient in nature and expensive, which limits the wide application of the Pt. Therefore, it is very important to develop an inexpensive, efficient and stable electrocatalyst for hydrogen evolution reaction. Although sulfides, selenides, phosphides, carbides, nitrides, and the like of transition metals such as molybdenum, tungsten, iron, cobalt, nickel, and the like are widely used in electrocatalytic hydrogen evolution reactions, these catalysts have far inferior performance to platinum-based catalysts, and are also inferior in stability in an acidic environment. Although ruthenium is also a precious metal, it is much less expensive than platinum, and the use of a small amount of ruthenium helps to obtain a cheap and efficient electrocatalyst. Most of ruthenium materials used for electrocatalytic hydrogen evolution reaction currently are metallic ruthenium and RuO2And RuPx nanoparticles, nanowires, and nanosheets are supported on different materials, such as graphene, carbon nitride, carbon nanotubes, TiO2 nanotube arrays, and the like. However, these materials cannot effectively exert electrocatalytic effect of the materials in hydrogen evolution reaction due to complicated synthesis method, large dosage and poor stability.
Disclosure of Invention
The invention aims to provide a preparation method of a PtRu catalyst, which is simple in synthesis method.
The preparation method of the PtRu catalyst disclosed by the invention adopts the technical scheme that:
a preparation method of the PtRu catalyst comprises the following steps:
s1, soaking the substrate material in ruthenium salt solution to load ruthenium on the substrate material, taking out the substrate material and drying;
s2, placing the dried substrate material in a muffle furnace for calcination to obtain RuO2A precursor;
s3 comparing RuO obtained in step S22The precursor is placed in a three-electrode electrolytic cell, and the electrolyte is sulfuric acid solution, Pt net, mercuric mercurous sulfate and obtained RuO2Precursors as counter, reference and working electrodes, RuO2The precursor electrodeposits Pt to obtain the PtRu catalyst.
Preferably, in step S1, the substrate material is carbon cloth, titanium foam, copper foam or nickel foam.
Preferably, in step S1, the ruthenium salt is ruthenium chloride, ruthenium iodide or ruthenium acetate.
Preferably, in the step S1, the concentration of the ruthenium salt solution is 0.001-5 mol/L.
Preferably, in step S1, the soaking time of the substrate material in the ruthenium salt solution is 1-120 min.
Preferably, in step S2, the calcination temperature of the dried substrate material in a muffle furnace is 200 to 600 ℃, and the calcination time is 5 to 120 min.
Preferably, in step S3, the concentration of the sulfuric acid solution is 0.01-5 mol/L.
Preferably, the mass ratio of Pt to Ru in the PtRu catalyst obtained in the step 3 is 0.01: 1-1: 1.
The preparation method of the PtRu catalyst disclosed by the invention has the beneficial effects that: the synthetic method is simple.
Another object of the present invention is to provide a PtRu catalyst, which is prepared by the above preparation method and has good catalytic stability in both acidic and alkaline electrolytes.
The invention also aims to disclose the application of the PtRu catalyst prepared by the preparation method as an electrolytic water hydrogen evolution electrode.
Drawings
FIG. 1 shows RuO prepared in example 12TEM images of the precursors;
fig. 2 is a TEM image of the PtRu catalyst prepared in example 1;
FIG. 3 shows PtRu catalysts prepared in examples 1 to 6 at 0.5M H2SO4A performance diagram of hydrogen evolution reaction in the electrolyte;
FIG. 4 is a graph showing the performance of the PtRu catalysts prepared in examples 1 to 6 in a hydrogen evolution reaction in a 1M KOH electrolyte;
FIG. 5 shows the PtRu catalyst prepared in example 4 at 0.5M H2SO4A stability performance diagram of hydrogen evolution reaction in the electrolyte;
fig. 6 is a graph showing the stability of the PtRu catalyst prepared in example 4 in the hydrogen evolution reaction in a 1M KOH electrolytic solution.
Detailed Description
The invention will be further elucidated and described with reference to the embodiments and drawings of the specification:
in the technical scheme, all the raw materials are commercially available.
Example 1:
(1) firstly, soaking the carbon cloth in 0.001mol/L ruthenium chloride aqueous solution for 1min, loading ruthenium chloride on the carbon cloth, and then drying at 60 ℃.
(2) Calcining the carbon cloth obtained in the step (1) in a muffle furnace, heating to 200 ℃ at a speed of 5 ℃/min, calcining in air for 5min, and obtaining a product after calcination, namely RuO2A precursor.
(3) And (3) placing the precursor obtained in the step (2) into a standard three-electrode electrolytic cell, wherein the electrolyte is a 0.01mol/L sulfuric acid solution. Pt net, mercury mercurous sulfate electrode and RuO obtained in step (2)2Precursors as counter, reference and working electrodes, respectively, in RuO2In-situ electro-depositing Pt on the precursor to obtain the PtRu catalyst, and controlling the deposition timeThe mass ratio of Pt to Ru is 0.01: 1.
FIG. 1 shows RuO2The transmission electron microscope shows that the single nano-particles have the particle size of about 3nm and are uniformly dispersed. FIG. 2 is a schematic representation of a RuO2The transmission electron microscope image of the PtRu catalyst after Pt is deposited on the precursor shows that the particle size and the morphology are basically unchanged before and after electrodeposition and are uniformly dispersed on the carbon cloth substrate.
Example 2:
(1) firstly, soaking titanium foam in 5mol/L ruthenium chloride aqueous solution for 120min, loading ruthenium chloride on the titanium foam, and then drying at 70 ℃.
(2) Calcining the foamed titanium obtained in the step (1) in a muffle furnace, heating to 600 ℃ at a speed of 5 ℃/min, calcining in air for 120min, and obtaining a product after calcination, namely RuO2A precursor.
(3) The RuO obtained in the step (2)2The precursor is placed in a standard three-electrode electrolytic cell, and the electrolyte is a 5mol/L sulfuric acid solution. Pt net, mercury mercurous sulfate electrode and RuO obtained in step (2)2Precursors as counter, reference and working electrodes, respectively, in RuO2In-situ electrodepositing Pt on the precursor to obtain the PtRu catalyst, and controlling the deposition time to ensure that the mass ratio of Pt to Ru is 1: 1.
Example 3:
(1) firstly, soaking foamed nickel in 0.1mol/L ruthenium iodide aqueous solution for 60min, loading ruthenium iodide on the foamed nickel, and then drying at 80 ℃.
(2) Calcining the foamed nickel obtained in the step (1) in a muffle furnace, heating to 400 ℃ at a speed of 5 ℃/min, calcining in air for 40min, and obtaining a product after calcination, namely RuO2A precursor.
(3) The RuO obtained in the step (2)2The precursor is placed in a standard three-electrode electrolytic cell, and the electrolyte is 1mol/L sulfuric acid solution. Pt net, mercury mercurous sulfate electrode and RuO obtained in step (2)2Precursors as counter, reference and working electrodes, respectively, in RuO2In-situ electrodepositing Pt on the precursor to obtain the PtRu catalyst, and controlling the deposition time to ensure that the mass ratio of Pt to Ru is 0.1: 1.
Example 4:
(1) firstly, soaking the carbon cloth in 0.2mol/L ruthenium chloride aqueous solution for 40min, loading ruthenium chloride on the carbon cloth, and then drying at 60 ℃.
(2) Calcining the carbon cloth obtained in the step (1) in a muffle furnace, heating to 300 ℃ at a speed of 5 ℃/min, calcining for 80min in air, wherein the calcined product is RuO2A precursor.
(3) The RuO obtained in the step (2)2The precursor is placed in a standard three-electrode electrolytic cell, and the electrolyte is 0.5mol/L sulfuric acid solution. Pt net, mercury mercurous sulfate electrode and RuO obtained in step (2)2Precursors as counter, reference and working electrodes, respectively, in RuO2In-situ electrodepositing Pt on the precursor to obtain the PtRu catalyst, and controlling the deposition time to ensure that the mass ratio of Pt to Ru is 0.5: 1.
Example 5:
(1) firstly, soaking foamed nickel in 0.3mol/L ruthenium chloride aqueous solution for 100min, loading ruthenium chloride on the foamed nickel, and then drying at 80 ℃.
(2) Calcining the foamed nickel obtained in the step (1) in a muffle furnace, heating to 400 ℃ at a speed of 5 ℃/min, calcining for 80min in air, wherein the calcined product is RuO2A precursor.
(3) The RuO obtained in the step (2)2The precursor is placed in a standard three-electrode electrolytic cell, and the electrolyte is a 5mol/L sulfuric acid solution. Pt net, mercury mercurous sulfate electrode and RuO obtained in step (2)2Precursors as counter, reference and working electrodes, respectively, in RuO2In-situ electrodepositing Pt on the precursor to obtain the PtRu catalyst, and controlling the deposition time to ensure that the mass ratio of Pt to Ru is 0.2: 1.
Example 6:
(1) firstly, soaking the copper foam in 0.5mol/L ruthenium acetate water solution for 120min, loading ruthenium acetate on the copper foam, and then drying at 80 ℃.
(2) Calcining the foamy copper obtained in the step (1) in a muffle furnace, heating to 300 ℃ at a speed of 5 ℃/min, calcining in air for 100min, and obtaining a product after calcination, namely RuO2A precursor.
(3) The RuO obtained in the step (2)2The precursor is placed in a standard three-electrode electrolytic cell, and the electrolyte is a 2mol/L sulfuric acid solution. Pt net, mercuric mercurous sulfate electrode and RuO obtained in step (2)2Precursors as counter, reference and working electrodes, respectively, in RuO2In-situ electrodepositing Pt on the precursor to obtain the PtRu catalyst, and controlling the deposition time to ensure that the mass ratio of Pt to Ru is 0.8: 1.
The PtRu catalysts prepared in examples 1-6 were used as working electrodes, carbon rods as counter electrodes, mercuric sulfate mercurous electrodes and mercuric oxide electrodes as reference electrodes in acidic and alkaline electrolytes, respectively, and electrochemical performance tests were performed using Chenghua 760E electrochemical workstation. The linear scan plot of the hydrogen evolution reaction in the acid electrolyte is shown in fig. 3, where the catalytic performance prepared in example 4 is best. The linear scan plot of the hydrogen evolution reaction in the alkaline electrolyte is shown in fig. 4, where the catalyst prepared in example 4 performs best.
In the above tests, the hydrogen evolution stability test result of the PtRu catalyst obtained in example 4 in the acidic electrolyte is shown in fig. 5, and the hydrogen evolution stability test result in the alkaline electrolyte is shown in fig. 6, indicating that the catalyst has good catalytic stability in both the acidic electrolyte and the alkaline electrolyte.
Therefore, the PtRu catalyst prepared by the method can be applied to serving as an electrolytic water hydrogen evolution electrode.
Finally, it should be noted that the above embodiments are only used for illustrating the technical solutions of the present invention, and not for limiting the protection scope of the present invention, although the present invention is described in detail with reference to the preferred embodiments, it should be understood by those skilled in the art that modifications or equivalent substitutions can be made on the technical solutions of the present invention without departing from the spirit and scope of the technical solutions of the present invention.

Claims (10)

1. A preparation method of a PtRu catalyst is characterized by comprising the following steps:
s1, soaking the substrate material in ruthenium salt solution to load ruthenium on the substrate material, taking out the substrate material and drying;
s2, placing the dried substrate material in a muffle furnace for calcination to obtain RuO2A precursor;
s3 comparing RuO obtained in step S22The precursor is placed in a three-electrode electrolytic cell, and the electrolyte is sulfuric acid solution, Pt net, mercuric mercurous sulfate and obtained RuO2Precursors as counter, reference and working electrodes, RuO2The precursor electrodeposits Pt to obtain the PtRu catalyst.
2. The method for producing a PtRu catalyst according to claim 1, wherein in step S1, the base material is carbon cloth, titanium foam, copper foam, or nickel foam.
3. The preparation method of the PtRu catalyst according to claim 1, wherein in step S1, the ruthenium salt is ruthenium chloride, ruthenium iodide or ruthenium acetate.
4. The method for producing a PtRu catalyst according to claim 1, wherein in step S1, the concentration of the ruthenium salt solution is 0.001 to 5 mol/L.
5. The method for preparing a PtRu catalyst according to claim 1, wherein in step S1, the immersion time of the base material in the ruthenium salt solution is 1 to 120 min.
6. The preparation method of the PtRu catalyst according to claim 1, wherein in step S2, the calcination temperature of the dried substrate material in a muffle furnace is 200-600 ℃, and the calcination time is 5-120 min.
7. The method for producing a PtRu catalyst according to claim 1, wherein in step S3, the concentration of the sulfuric acid solution is 0.01 to 5 mol/L.
8. The method of producing a PtRu catalyst according to claim 1, wherein the mass ratio of Pt to Ru in the PtRu catalyst obtained in step S3 is 0.01:1 to 1: 1.
9. A PtRu catalyst, characterized by being produced by the production method for a PtRu catalyst according to any one of claims 1 to 8.
10. Use of the PtRu catalyst prepared by the method for preparing a PtRu catalyst according to any one of claims 1 to 8 as a hydrogen evolution electrode in electrolytic water.
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CN111167442A (en) * 2020-01-05 2020-05-19 复旦大学 Ruthenium-iridium composite oxide material doped with hydrated metal and preparation method and application thereof
CN113684498B (en) * 2021-08-05 2023-01-24 中国科学技术大学 Preparation method and application of monatomic alloy catalyst
CN113603191B (en) * 2021-08-23 2022-11-01 中国科学院生态环境研究中心 Metal ruthenium-based electrode and preparation method and application thereof
CN116103693B (en) * 2022-11-25 2023-09-12 东莞理工学院 Hydrogen evolution electrode, preparation method thereof and application thereof in hydrogen production by water electrolysis
CN116062722B (en) * 2023-02-24 2024-08-06 海卓动力(北京)能源科技有限公司 Catalyst and preparation method and application thereof
CN116083952B (en) * 2023-03-28 2023-06-13 西南石油大学 Cu (copper) alloy 3 Ti nano-sheet loaded Ti-doped CuO/Ru hydrogen evolution reaction catalyst and preparation method thereof

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