CN117568843A - Selenium-defect-enriched tin diselenide nanosheet electrocatalyst and preparation method and application thereof - Google Patents

Selenium-defect-enriched tin diselenide nanosheet electrocatalyst and preparation method and application thereof Download PDF

Info

Publication number
CN117568843A
CN117568843A CN202311455651.5A CN202311455651A CN117568843A CN 117568843 A CN117568843 A CN 117568843A CN 202311455651 A CN202311455651 A CN 202311455651A CN 117568843 A CN117568843 A CN 117568843A
Authority
CN
China
Prior art keywords
selenium
tin
tin diselenide
nanosheet electrocatalyst
enriched
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
Application number
CN202311455651.5A
Other languages
Chinese (zh)
Inventor
侯阳
赵紫琳
杨彬
雷乐成
李中坚
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Donghai Laboratory
Zhejiang University ZJU
Original Assignee
Donghai Laboratory
Zhejiang University ZJU
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Donghai Laboratory, Zhejiang University ZJU filed Critical Donghai Laboratory
Priority to CN202311455651.5A priority Critical patent/CN117568843A/en
Publication of CN117568843A publication Critical patent/CN117568843A/en
Pending legal-status Critical Current

Links

Classifications

    • 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
    • C25B11/051Electrodes formed of electrocatalysts on a substrate or carrier
    • C25B11/073Electrodes formed of electrocatalysts on a substrate or carrier characterised by the electrocatalyst material
    • C25B11/075Electrodes formed of electrocatalysts on a substrate or carrier characterised by the electrocatalyst material consisting of a single catalytic element or catalytic compound
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B3/00Electrolytic production of organic compounds
    • C25B3/01Products
    • C25B3/07Oxygen containing compounds

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Catalysts (AREA)

Abstract

The invention discloses a preparation method of a tin diselenide nanosheet electrocatalyst rich in selenium defects, which comprises the following steps: and dissolving selenium dioxide and metallic tin salt, adding hydrazine hydrate solution, stirring and mixing, and performing hydrothermal reaction to obtain the selenium-enriched tin diselenide nanosheet electrocatalyst. The invention also discloses the tin diselenide nanosheet electrocatalyst rich in selenium defects obtained by the preparation method and application of the tin diselenide nanosheet electrocatalyst serving as a working electrode in formic acid electrosynthesis. The catalyst provided by the invention realizes high selectivity of HCOOH electrosynthesis in alkaline, neutral and acidic electrolytes respectively, and the HCOOH partial current density reaches the industrial level under the corresponding pH condition, so that the catalyst fully shows excellent HCOOH electrosynthesis performance in the full pH range.

Description

Selenium-defect-enriched tin diselenide nanosheet electrocatalyst and preparation method and application thereof
Technical Field
The invention relates to the technical field of electrocatalysts, in particular to a tin diselenide nanosheet electrocatalyst rich in selenium defects, and a preparation method and application thereof.
Background
Carbon dioxide (CO) using renewable energy sources 2 ) Among various reduction products, formic acid (HCOOH) is considered as one of the most technically economical products, and has been widely used in practical applications. Several major p-region metal main group catalysts have been reported to date, including Sn, in, bi, and the like, and a series of corresponding metal oxides (such as tin oxide and indium oxide) for the electroreduction of CO 2 Synthesizing HCOOH. Wherein, because of low cost of metal tin-based material, the adsorption energy of OOCH intermediate in the process of electrosynthesis of HCOOH is moderate, so that the catalyst is widely applied to the electroreduction of CO 2 Synthesizing HCOOH. However, the metallic tin-based catalysts reported to date do @ achieve high selectivity commercial current densities>200mA cm -2 ) The aspects of HCOOH electrosynthesis still face significant challenges.
Currently, HCOOH electrosynthesis is mostly carried out in alkaline or neutral electrolytes, and thus, the formation of carbonate byproducts is unavoidable, leading to CO 2 The utilization efficiency is lowered. The use of an acidic electrolyte is one of the effective methods for solving these problems. However, due to the electroreduction of CO 2 Competitive hydrogen evolution side reactions and unavoidable proton concentration changes in the process, achieving sustained effective CO in acidic electrolytes 2 Transformation still faces a significant challenge. Therefore, in industrial applications, it is highly necessary to develop ideal catalysts that work well over the full pH range. The Chinese patent document with publication number CN115584522A discloses a preparation method of a three-dimensional porous electrode and an acidic electrocatalytic CO thereof 2 The application of preparing formic acid by reduction is that a catalyst, a polymer and an organic solvent are uniformly mixed to prepare composite slurry, the slurry is uniformly coated on carbon cloth by a scraper to obtain an unformed blank, and finally a three-dimensional porous electrode is obtained by drying treatment, so that HCOOH is prepared by electric reduction under the acidic condition that the pH is less than 3.77.
The formation of OOCH intermediates is typically the rate-determining reaction step due to slow reaction kinetics during proton formation and transport. Thus, accelerating proton generation and transfer is an effective method of increasing OOCH/HCOOH generation rate. The introduction of defective structures is considered to be one of the most direct and effective methods for regulating metal electrons and surface structures, and has been studied extensively in recent years. The Chinese patent document of publication No. CN116103680A discloses an oxygen vacancy-enriched bismuth carbonate electrocatalyst and a preparation method thereof, bismuth salt is dissolved in glycol and aqueous solution, a proper amount of auxiliary conductive salt is added, and then the bismuth salt is refrigerated to obtain electrolyte, and electrochemical deposition is carried out on a working electrode by using a constant current method to obtain oxygen vacancy-enriched bismuth carbonate nanosheets, wherein the introduction of oxygen vacancies improves the conductivity of bismuth carbonate, and improves the water splitting ability of bismuth carbonate and the intrinsic activity of HCOOH synthesis.
Although CO is reduced electrically for different electrolyte environments 2 Research on the synthesis of HCOOH has been greatly advanced, but industrial current density achieved over the full pH range>200mA cm -2 ) The HCOOH electrosynthesis of (c) still faces the problem of low selectivity.
Disclosure of Invention
The invention aims to provide a preparation method of a tin diselenide nanosheet electrocatalyst rich in selenium defects, and the prepared catalyst is rich in selenium defects and shows excellent catalysis performance of HCOOH electrosynthesis.
In order to achieve the above purpose, the invention adopts the following technical scheme:
a method for preparing a tin diselenide nanosheet electrocatalyst rich in selenium defects, the method comprising the steps of: and dissolving selenium dioxide and metallic tin salt, adding hydrazine hydrate solution, stirring and mixing, and performing hydrothermal reaction to obtain the selenium-enriched tin diselenide nanosheet electrocatalyst.
The preparation principle of the tin diselenide nanosheet electrocatalyst rich in selenium defects provided by the invention is as follows: adding a reducing reagent hydrazine hydrate into the mixed solution of uniformly dispersed selenium dioxide and metallic tin salt, and adding Sn in the solution into hydrazine hydrate molecules with strong reducibility 2+ And Se (Se) 4+ Reduced to atoms with high reflectionThe Sn atoms and Se atoms that should be active combine to form a tin diselenide molecule, accompanied by the formation of selenium defects. The selenium defect is introduced to transfer more electrons from Se sites to Sn sites, so that dissociation of water molecules is effectively accelerated, proton transfer rate is improved, and CO is accelerated 2 High efficiency conversion at tin active site.
The metallic tin salt is a soluble salt, preferably the metallic tin salt is stannous chloride dihydrate.
The molar ratio of the selenium dioxide to the metallic tin salt is 1.5-2.5:1. According to the invention, the tin diselenide nano-sheets with different purity and rich selenium defects are prepared by changing the dosage of selenium dioxide. When the molar concentration of selenium dioxide is too low, the purity of the resulting tin diselenide is reduced, and the presence of heterogeneous tin is observed for the electroreduction of CO 2 The performance of synthesizing HCOOH is not obviously improved; when the molar concentration of selenium dioxide is too high, a selenous phase can appear, so that the electrosynthesis performance of HCOOH is obviously reduced.
Further, dissolving selenium dioxide and metallic tin salt in water to obtain a mixed solution, wherein the mass concentration of the selenium dioxide is 7.4-22.2 g L -1 The mass concentration of the tin salt is 15.0. 15.0g L -1 . Preferably, the mass concentration of the selenium dioxide is 14.8g L -1
Wherein, the selenium dioxide and the metallic tin salt are dissolved in a certain amount of aqueous solution, the reaction temperature is room temperature, and the stirring time is 10-20 min. Preferably, the stirring time is 20min.
Further, the mass concentration of the hydrazine hydrate is 54.8g L in the mixed solution after the hydrazine hydrate is added -1
And after the mixed solution of the selenium dioxide and the metallic tin salt is added into the hydrazine hydrate solution, the reaction temperature is normal temperature, and the stirring time is 3-8 min. Too long stirring time can affect the morphology of tin diselenide to be uneven and the formation of selenium defects, thereby affecting the performance of the electrocatalyst. Preferably, the stirring time is 3 minutes.
The hydrothermal reaction temperature is 160-200 ℃. The selenium defects with different contents are prepared by changing the hydrothermal reaction temperatureTin diselenide nanosheets of (a). When the hydrothermal reaction temperature is too low, tin diselenide nano-sheets rich in selenium defects are not easy to form; when the hydrothermal reaction temperature is too high, the nano-sheet of the tin diselenide is easy to generate crystal phase transition at high temperature, so that CO is electrically reduced 2 The performance of preparing HCOOH is reduced.
Preferably, the molar ratio of the selenium dioxide to the metallic tin salt is 1.5-2:1, and the hydrothermal reaction temperature is 180-200 ℃. By limiting the molar ratio and the reaction temperature, the purity and the content of selenium defects in the prepared tin diselenide nano-sheet are more beneficial to improving the electric reduction CO 2 Selectivity for the preparation of HCOOH.
The invention also provides the tin diselenide nanosheet electrocatalyst rich in selenium defects, which is obtained by the preparation method.
The abundant selenium defects in the catalyst exist in the tin diselenide nanosheets, and the atomic ratio of selenium to tin in the tin diselenide nanosheets electrocatalyst is 1.8-2.0:1.
The invention also provides an application of the selenium-enriched tin diselenide nanosheet electrocatalyst serving as a working electrode in formic acid electrosynthesis.
Furthermore, the tin diselenide nanosheet electrocatalyst rich in selenium defects is used as a working electrode in formic acid electrosynthesis under the condition of industrial-grade current density in a full pH range.
The tin diselenide nanosheet electrocatalyst rich in selenium defects provided by the invention has the following advantages under the industrial current density>200mA cm -2 ) High selectivity performance is achieved. Wherein the highest HCOOH selectivities in alkaline, neutral and acidic electrolytes are 94.1%, 81.7% and 78.1%, respectively, and the peak partial current densities of HCOOH are 800, 568 and 495mA cm, respectively -2 The electrocatalytic performance is far superior to that of commercial tin diselenide catalysts.
The tin diselenide nanosheet electrocatalyst rich in selenium defects provided by the invention can effectively improve the adsorption and dissociation capacities of the tin diselenide nanosheet electrocatalyst on water molecules, and accelerate the proton transfer and intermediate formation rate, so that the electrocatalyst activity of the tin diselenide nanosheet electrocatalyst is further improved, and the tin diselenide nanosheet electrocatalyst is very significant in preparing HCOOH under industrial conditions.
Compared with the prior art, the invention has the following beneficial effects:
(1) The tin diselenide nanosheet electrocatalyst rich in selenium defects provided by the invention realizes high-selectivity CO 2 Catalytic conversion to HCOOH, and has a broad operable pH window (2.0-14.0). Realizes the electrosynthesis of HCOOH with industrial current density under different pH environments, and provides possibility for further industrial large-scale application.
(2) According to the selenium-defect-enriched tin diselenide nanosheet electrocatalyst provided by the invention, through the introduction of selenium defects, the electronic structure of tin diselenide is effectively regulated, so that the electron density around tin sites is more abundant, water molecules are effectively accelerated to dissociate more protons, further the formation of an intermediate COOH is accelerated, and finally the synthesis process of HCOOH is accelerated.
Drawings
FIG. 1 is a SEM image of the catalyst prepared in example 1;
FIG. 2 is an X-ray diffraction XRD pattern of the catalyst prepared in example 1;
FIG. 3 is an electron paramagnetic resonance EPR plot of the catalysts prepared in example 1 and examples 2-3;
FIG. 4 shows the electrical reduction of CO in the application example of the catalyst prepared in example 1 2 Faradaic efficiency of HCOOH preparation.
FIG. 5 shows the electroreduction of CO in the application of the catalysts prepared in example 1 and examples 2 to 3 2 Faradaic efficiency of HCOOH preparation.
FIG. 6 shows the electroreduction of CO at pH=14.0 in the examples of application for the catalysts prepared in example 1 and examples 4 to 5 2 Faradaic efficiency of HCOOH preparation.
Detailed Description
The present invention will be described in further detail with reference to the following examples in order to make the objects, technical solutions and advantages of the present invention more apparent. It should be understood that the specific embodiments described herein are for purposes of illustration only and are not intended to limit the scope of the invention. Modifications and equivalents will occur to those skilled in the art upon understanding the present teachings without departing from the spirit and scope of the present teachings. The raw materials used in the following embodiments are all commercially available.
Example 1
(1) 443.8mg of selenium dioxide solid particles and 451.3mg of stannous chloride dihydrate solid particles are weighed and dissolved in 30mL of deionized water solution, and stirred at normal temperature for 20min for later use;
(2) Adding 2mL of the solution prepared in the step (1) into 85wt.% hydrazine hydrate solution, and stirring for 5min; transferring the obtained mixed solution into a 50mL hydrothermal kettle, and carrying out hydrothermal reaction for 24 hours at 180 ℃;
(3) And (3) centrifugally separating the initial product obtained in the step (2), respectively washing with water and ethanol for more than 3 times, and finally drying in a vacuum oven at 60 ℃ for 12 hours to obtain the tin diselenide nano-sheet catalyst rich in selenium defects.
The microscopic morphology of the prepared catalyst is observed through a scanning electron microscope SEM, and the SEM result is shown in figure 1, so that the morphological structure of the tin diselenide catalyst rich in selenium defects is a hexagonal lamellar structure, and the thickness of the lamellar layer is about 50nm. The X-ray diffraction XRD pattern of the selenium-defect-enriched tin diselenide prepared in this example is shown in fig. 2, the characteristic peak of the crystal phase of the tin diselenide can be seen, the electron paramagnetic resonance EPR pattern is shown in fig. 3, and the existence of the selenium defect can be clearly seen, which indicates the successful preparation of the selenium-defect-enriched tin diselenide nanosheet electrocatalyst.
Example 2
The catalyst of example 2 was obtained by changing the hydrothermal reaction temperature in step (2) to 160℃according to the preparation process of example 1.
Example 3
The catalyst of example 3 was obtained by changing the hydrothermal reaction temperature in step (2) to 200℃according to the preparation process of example 1.
Example 4
According to the preparation process of example 1, the mass of the selenium dioxide solid particles in the step (1) is changed to 332.8mg to obtain the catalyst of example 4.
Example 5
According to the preparation process of example 1, the mass of the selenium dioxide solid particles in the step (1) is changed to 554.7mg to obtain the catalyst of example 5.
Application example HCOOH electrosynthesis at Industrial grade Current Density in full pH Range
First, 10mg of the catalyst prepared above was dispersed in 1000. Mu.L of a 9:1 ethanol/Nafion volume ratio dispersion, and then 100. Mu.L of the dispersion was sprayed to 0.5 x 0.5cm 2 After natural drying, it is placed as a working electrode in a three-electrode flow cell measuring device consisting of two compartments separated by an anion exchange membrane. Wherein, 1.0M KOH solution is used as alkaline electrolyte, and 1.0M KHCO is used 3 Solution as neutral electrolyte, 0.5. 0.5M K 2 SO 4 And H 2 SO 4 The mixed solution serves as an acidic electrolyte. The counter electrode of the alkaline electrolyte and the neutral electrolyte is foam nickel, the counter electrode of the acidic electrolyte is a platinum sheet, and the reference electrode is a silver/silver chloride electrode.
Cyclic Voltammetry (CV) activation: the electrochemical workstation of Shanghai Chenhua CHI 760E is used, a CV program is adopted, the test interval is between 0 and minus 1.4V vs. RHE, and the sweeping speed is 50mV s -1 The electrode reaches a stable state after 40 circles of cyclic scanning.
Linear Sweep Voltammetry (LSV) test: after CV activation, switching the program to LSV program, wherein the test interval is 0 to-1.4V vs. RHE, and the sweeping speed is 5mV s -1
Faraday Efficiency (FE) test: the switching procedure is a constant current voltage-time test, during which the gas chromatography is used to determine the gas product concentration and calculate FE of the product. On-line quantification by gas chromatography (GC, fuli 9790 II) using 1 And (3) analyzing the FE of the liquid product by using an H nuclear magnetic resonance analyzer, and measuring by using an internal standard method, namely using dimethyl sulfoxide as a standard.
As shown in FIG. 4, the selenium-enriched tin diselenide nanosheet electrocatalyst prepared in example 1 exhibited excellent HCOOH electrosynthesis performance over the full pH range, achieving 94.1%, 81.7% and 78.1% selectivities of HCOOH in alkaline, neutral and acidic electrolytes, respectively, corresponding HCOOH partial current densities of 800, 568 and 495mA cm -2 Reaching the industrial level.
Comparing the HCOOH Faraday efficiencies of the electrocatalysts prepared in example 1 and examples 2-3 under different pH environments at-0.8V vs. RHE, the results are shown in FIG. 5, wherein the HCOOH electrosynthesis performance of the tin diselenide nanosheet electrocatalysts rich in selenium defects prepared in example 1 is far better than that of examples 2 and 3 over the full pH range.
Comparing the electrosynthesis performance of HCOOH with the electrocatalysts prepared in examples 1 and 4-5 at ph=14.0, the result is that, as shown in fig. 6, the electrosynthesis selectivity of the tin diselenide nanosheet electrocatalyst enriched in selenium defects prepared in example 1 is far higher than that of examples 4 and 5.

Claims (8)

1. The preparation method of the tin diselenide nanosheet electrocatalyst rich in selenium defects is characterized by comprising the following steps of: and dissolving selenium dioxide and metallic tin salt, adding hydrazine hydrate solution, stirring and mixing, and performing hydrothermal reaction to obtain the selenium-enriched tin diselenide nanosheet electrocatalyst.
2. The method for preparing the selenium-defect-enriched tin diselenide nanosheet electrocatalyst according to claim 1, wherein the molar ratio of selenium dioxide to metallic tin salt is 1.5-2.5:1.
3. The method for preparing the selenium-defect-enriched tin diselenide nanosheet electrocatalyst according to claim 1, wherein the hydrothermal reaction temperature is 160-200 ℃.
4. The method for preparing the selenium-defect-enriched tin diselenide nanosheet electrocatalyst according to claim 1, wherein the molar ratio of selenium dioxide to metallic tin salt is 1.5-2:1, and the hydrothermal reaction temperature is 180-200 ℃.
5. A tin nanosheet electrocatalyst enriched in selenium defects obtainable by the process according to any one of claims 1 to 4.
6. The selenium-defect-enriched tin diselenide nanosheet electrocatalyst according to claim 5, wherein the atomic ratio of selenium to tin in the tin diselenide nanosheet electrocatalyst is from 1.8 to 2.0:1.
7. Use of the selenium-enriched defective tin diselenide nanosheet electrocatalyst according to claim 5 or 6 as a working electrode in the electrosynthesis of formic acid.
8. The use of the selenium-rich and defective tin diselenide nanosheet electrocatalyst according to claim 7, wherein the selenium-rich and defective tin diselenide nanosheet electrocatalyst is used as a working electrode for formic acid electrosynthesis at industrial grade current densities in the full pH range.
CN202311455651.5A 2023-11-03 2023-11-03 Selenium-defect-enriched tin diselenide nanosheet electrocatalyst and preparation method and application thereof Pending CN117568843A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202311455651.5A CN117568843A (en) 2023-11-03 2023-11-03 Selenium-defect-enriched tin diselenide nanosheet electrocatalyst and preparation method and application thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202311455651.5A CN117568843A (en) 2023-11-03 2023-11-03 Selenium-defect-enriched tin diselenide nanosheet electrocatalyst and preparation method and application thereof

Publications (1)

Publication Number Publication Date
CN117568843A true CN117568843A (en) 2024-02-20

Family

ID=89861507

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202311455651.5A Pending CN117568843A (en) 2023-11-03 2023-11-03 Selenium-defect-enriched tin diselenide nanosheet electrocatalyst and preparation method and application thereof

Country Status (1)

Country Link
CN (1) CN117568843A (en)

Similar Documents

Publication Publication Date Title
CN111672514A (en) Bifunctional electrocatalytic material and preparation method and application thereof
CN113828300B (en) Preparation method of metal doped bismuth layered oxide and electrocatalytic reduction of CO 2 Application in (a)
CN112481653B (en) Defect-rich molybdenum-doped cobalt selenide/nano carbon electrocatalyst and preparation method and application thereof
CN113235104B (en) ZIF-67-based lanthanum-doped cobalt oxide catalyst and preparation method and application thereof
CN113249739B (en) Metal phosphide-loaded monatomic catalyst, preparation method thereof and application of metal phosphide-loaded monatomic catalyst as hydrogen evolution reaction electrocatalyst
CN110560094B (en) Preparation method of 3D porous cobalt-tin-molybdenum trimetal catalyst
CN113789545B (en) Electrolytic water catalyst and preparation method and application thereof
CN112921351B (en) Preparation method and application of self-supporting catalytic electrode
CN117089881A (en) Preparation method of Pt nanoparticle modified bimetallic LDH catalyst and industrial current density electrolyzed water application thereof
CN112458483B (en) Preparation method of NiFe LDH @ Super-P composite electro-catalytic material
CN115404513A (en) Carbon-coated heterostructure electrocatalyst and preparation and application thereof
CN114774983A (en) Ultra-small Ru nanocluster loaded on MoO3-xDouble-function composite material of nanobelt and preparation method and application thereof
CN117568843A (en) Selenium-defect-enriched tin diselenide nanosheet electrocatalyst and preparation method and application thereof
CN113774425A (en) Preparation method and application of Ru-modified FeCo @ NF electrocatalyst
CN113293407A (en) Iron-rich nanobelt oxygen evolution electrocatalyst and preparation method thereof
CN117904673B (en) Electrocatalyst and preparation and application thereof
CN114045514B (en) Preparation method of V@CoxP catalyst
CN115094475B (en) Electrode material with high-performance oxygen evolution catalytic activity and preparation method thereof
CN115652357B (en) Sulfur-doped yttrium ruthenate, preparation method thereof and oxygen evolution reaction electrode
CN114892212B (en) Preparation method of sulfur-doped nickel-based metal organic frame electrode material with bionic active domain, product and application thereof
CN114717599B (en) Ruthenium-supported nickel metal three-dimensional carbon sphere electrocatalyst and preparation method and application thereof
CN111774071B (en) Ternary metal sulfide nanosheet material, preparation method thereof and application of ternary metal sulfide nanosheet material in water electrolysis
CN114214636B (en) Method for preparing cobalt-based nanosheet self-supporting electrode by selenium-containing ligand and application of cobalt-based nanosheet self-supporting electrode
CN118326441A (en) Preparation method and application of Y-composite Cu-MOF carbon dioxide reduction electrocatalyst
CN118461061A (en) Ru-Sn-Ce ternary composite material, preparation method thereof and application of Ru-Sn-Ce ternary composite material as electrocatalyst for oxygen evolution reaction

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