CN115896810A - Noble metal monatomic catalyst based on high entropy effect and preparation method thereof - Google Patents
Noble metal monatomic catalyst based on high entropy effect and preparation method thereof Download PDFInfo
- Publication number
- CN115896810A CN115896810A CN202211479510.2A CN202211479510A CN115896810A CN 115896810 A CN115896810 A CN 115896810A CN 202211479510 A CN202211479510 A CN 202211479510A CN 115896810 A CN115896810 A CN 115896810A
- Authority
- CN
- China
- Prior art keywords
- noble metal
- mol
- preparation
- concentration
- monatomic catalyst
- 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.)
- Granted
Links
- 239000003054 catalyst Substances 0.000 title claims abstract description 62
- 229910000510 noble metal Inorganic materials 0.000 title claims abstract description 57
- 230000000694 effects Effects 0.000 title claims abstract description 26
- 238000002360 preparation method Methods 0.000 title claims abstract description 19
- 229910052751 metal Inorganic materials 0.000 claims abstract description 23
- 239000002184 metal Substances 0.000 claims abstract description 17
- 229910052697 platinum Inorganic materials 0.000 claims abstract description 12
- 229910052737 gold Inorganic materials 0.000 claims abstract description 6
- 238000000034 method Methods 0.000 claims abstract description 4
- 229910052748 manganese Inorganic materials 0.000 claims abstract description 3
- 229910052759 nickel Inorganic materials 0.000 claims abstract description 3
- 239000000243 solution Substances 0.000 claims description 26
- 238000006243 chemical reaction Methods 0.000 claims description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 17
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 claims description 14
- GNTDGMZSJNCJKK-UHFFFAOYSA-N divanadium pentaoxide Chemical compound O=[V](=O)O[V](=O)=O GNTDGMZSJNCJKK-UHFFFAOYSA-N 0.000 claims description 14
- VKYKSIONXSXAKP-UHFFFAOYSA-N hexamethylenetetramine Chemical compound C1N(C2)CN3CN1CN2C3 VKYKSIONXSXAKP-UHFFFAOYSA-N 0.000 claims description 14
- 238000003760 magnetic stirring Methods 0.000 claims description 12
- 229910052938 sodium sulfate Inorganic materials 0.000 claims description 12
- 235000011152 sodium sulphate Nutrition 0.000 claims description 12
- 239000002243 precursor Substances 0.000 claims description 11
- 239000002253 acid Substances 0.000 claims description 10
- 238000002156 mixing Methods 0.000 claims description 10
- 238000001027 hydrothermal synthesis Methods 0.000 claims description 9
- 239000000843 powder Substances 0.000 claims description 9
- 150000003839 salts Chemical class 0.000 claims description 9
- PTFCDOFLOPIGGS-UHFFFAOYSA-N Zinc dication Chemical compound [Zn+2] PTFCDOFLOPIGGS-UHFFFAOYSA-N 0.000 claims description 7
- 238000001816 cooling Methods 0.000 claims description 7
- 239000012153 distilled water Substances 0.000 claims description 7
- 238000001035 drying Methods 0.000 claims description 7
- 235000010299 hexamethylene tetramine Nutrition 0.000 claims description 7
- 239000002904 solvent Substances 0.000 claims description 7
- 238000009210 therapy by ultrasound Methods 0.000 claims description 7
- 229910001456 vanadium ion Inorganic materials 0.000 claims description 7
- 238000005406 washing Methods 0.000 claims description 7
- 239000012266 salt solution Substances 0.000 claims description 6
- 229910000337 indium(III) sulfate Inorganic materials 0.000 claims description 4
- XGCKLPDYTQRDTR-UHFFFAOYSA-H indium(iii) sulfate Chemical compound [In+3].[In+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O XGCKLPDYTQRDTR-UHFFFAOYSA-H 0.000 claims description 4
- YBCAZPLXEGKKFM-UHFFFAOYSA-K ruthenium(iii) chloride Chemical compound [Cl-].[Cl-].[Cl-].[Ru+3] YBCAZPLXEGKKFM-UHFFFAOYSA-K 0.000 claims description 4
- XURCIPRUUASYLR-UHFFFAOYSA-N Omeprazole sulfide Chemical compound N=1C2=CC(OC)=CC=C2NC=1SCC1=NC=C(C)C(OC)=C1C XURCIPRUUASYLR-UHFFFAOYSA-N 0.000 claims description 3
- PSCMQHVBLHHWTO-UHFFFAOYSA-K indium(iii) chloride Chemical compound Cl[In](Cl)Cl PSCMQHVBLHHWTO-UHFFFAOYSA-K 0.000 claims description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 2
- 229910002651 NO3 Inorganic materials 0.000 claims description 2
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 claims description 2
- NHNBFGGVMKEFGY-UHFFFAOYSA-N nitrate group Chemical group [N+](=O)([O-])[O-] NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 claims description 2
- 230000035484 reaction time Effects 0.000 claims description 2
- 239000011701 zinc Substances 0.000 claims description 2
- 238000006555 catalytic reaction Methods 0.000 abstract description 4
- 239000000758 substrate Substances 0.000 abstract description 4
- 239000002131 composite material Substances 0.000 abstract description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 abstract description 2
- -1 oxygen ions Chemical class 0.000 description 43
- 239000011259 mixed solution Substances 0.000 description 20
- 239000003153 chemical reaction reagent Substances 0.000 description 15
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 15
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 9
- 229910052739 hydrogen Inorganic materials 0.000 description 9
- 239000001257 hydrogen Substances 0.000 description 9
- 230000004075 alteration Effects 0.000 description 8
- 230000003197 catalytic effect Effects 0.000 description 8
- 230000001276 controlling effect Effects 0.000 description 8
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 8
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Substances [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 7
- 238000000634 powder X-ray diffraction Methods 0.000 description 7
- 238000012360 testing method Methods 0.000 description 7
- 238000005868 electrolysis reaction Methods 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 6
- 239000000463 material Substances 0.000 description 6
- 238000003917 TEM image Methods 0.000 description 5
- 238000012937 correction Methods 0.000 description 5
- 239000011572 manganese Substances 0.000 description 5
- 239000002135 nanosheet Substances 0.000 description 5
- 238000007789 sealing Methods 0.000 description 5
- 238000001228 spectrum Methods 0.000 description 5
- 229910052782 aluminium Inorganic materials 0.000 description 4
- 230000005540 biological transmission Effects 0.000 description 4
- 229910001429 cobalt ion Inorganic materials 0.000 description 4
- XLJKHNWPARRRJB-UHFFFAOYSA-N cobalt(2+) Chemical compound [Co+2] XLJKHNWPARRRJB-UHFFFAOYSA-N 0.000 description 4
- 239000010931 gold Substances 0.000 description 4
- 229910001449 indium ion Inorganic materials 0.000 description 4
- 229910052742 iron Inorganic materials 0.000 description 4
- VCJMYUPGQJHHFU-UHFFFAOYSA-N iron(3+);trinitrate Chemical compound [Fe+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O VCJMYUPGQJHHFU-UHFFFAOYSA-N 0.000 description 4
- 229910001437 manganese ion Inorganic materials 0.000 description 4
- 238000001000 micrograph Methods 0.000 description 4
- 229910001453 nickel ion Inorganic materials 0.000 description 4
- JIAARYAFYJHUJI-UHFFFAOYSA-L zinc dichloride Chemical compound [Cl-].[Cl-].[Zn+2] JIAARYAFYJHUJI-UHFFFAOYSA-L 0.000 description 4
- ONDPHDOFVYQSGI-UHFFFAOYSA-N zinc nitrate Chemical compound [Zn+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O ONDPHDOFVYQSGI-UHFFFAOYSA-N 0.000 description 4
- JPVYNHNXODAKFH-UHFFFAOYSA-N Cu2+ Chemical compound [Cu+2] JPVYNHNXODAKFH-UHFFFAOYSA-N 0.000 description 3
- WAEMQWOKJMHJLA-UHFFFAOYSA-N Manganese(2+) Chemical compound [Mn+2] WAEMQWOKJMHJLA-UHFFFAOYSA-N 0.000 description 3
- RLNMYVSYJAGLAD-UHFFFAOYSA-N [In].[Pt] Chemical compound [In].[Pt] RLNMYVSYJAGLAD-UHFFFAOYSA-N 0.000 description 3
- FTJAWXAYBYAEJR-UHFFFAOYSA-N [Ru].[In] Chemical compound [Ru].[In] FTJAWXAYBYAEJR-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 239000010949 copper Substances 0.000 description 3
- 229910001431 copper ion Inorganic materials 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 230000001105 regulatory effect Effects 0.000 description 3
- 229910052707 ruthenium Inorganic materials 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 229910017566 Cu-Mn Inorganic materials 0.000 description 2
- 229910017871 Cu—Mn Inorganic materials 0.000 description 2
- VEQPNABPJHWNSG-UHFFFAOYSA-N Nickel(2+) Chemical compound [Ni+2] VEQPNABPJHWNSG-UHFFFAOYSA-N 0.000 description 2
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- ORTQZVOHEJQUHG-UHFFFAOYSA-L copper(II) chloride Chemical compound Cl[Cu]Cl ORTQZVOHEJQUHG-UHFFFAOYSA-L 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- RUTXIHLAWFEWGM-UHFFFAOYSA-H iron(3+) sulfate Chemical compound [Fe+3].[Fe+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O RUTXIHLAWFEWGM-UHFFFAOYSA-H 0.000 description 2
- 229910000360 iron(III) sulfate Inorganic materials 0.000 description 2
- 238000011068 loading method Methods 0.000 description 2
- 229940099596 manganese sulfate Drugs 0.000 description 2
- 235000007079 manganese sulphate Nutrition 0.000 description 2
- 239000011702 manganese sulphate Substances 0.000 description 2
- SQQMAOCOWKFBNP-UHFFFAOYSA-L manganese(II) sulfate Chemical compound [Mn+2].[O-]S([O-])(=O)=O SQQMAOCOWKFBNP-UHFFFAOYSA-L 0.000 description 2
- 239000002105 nanoparticle Substances 0.000 description 2
- KBJMLQFLOWQJNF-UHFFFAOYSA-N nickel(ii) nitrate Chemical compound [Ni+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O KBJMLQFLOWQJNF-UHFFFAOYSA-N 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 230000010287 polarization Effects 0.000 description 2
- 239000010970 precious metal Substances 0.000 description 2
- 229910001925 ruthenium oxide Inorganic materials 0.000 description 2
- WOCIAKWEIIZHES-UHFFFAOYSA-N ruthenium(iv) oxide Chemical compound O=[Ru]=O WOCIAKWEIIZHES-UHFFFAOYSA-N 0.000 description 2
- 235000005074 zinc chloride Nutrition 0.000 description 2
- 239000011592 zinc chloride Substances 0.000 description 2
- BNGXYYYYKUGPPF-UHFFFAOYSA-M (3-methylphenyl)methyl-triphenylphosphanium;chloride Chemical compound [Cl-].CC1=CC=CC(C[P+](C=2C=CC=CC=2)(C=2C=CC=CC=2)C=2C=CC=CC=2)=C1 BNGXYYYYKUGPPF-UHFFFAOYSA-M 0.000 description 1
- 229910021578 Iron(III) chloride Inorganic materials 0.000 description 1
- 229910021380 Manganese Chloride Inorganic materials 0.000 description 1
- GLFNIEUTAYBVOC-UHFFFAOYSA-L Manganese chloride Chemical compound Cl[Mn]Cl GLFNIEUTAYBVOC-UHFFFAOYSA-L 0.000 description 1
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 1
- MBGDOZCTEJQOJU-UHFFFAOYSA-N [In].[Pt].[Au] Chemical compound [In].[Pt].[Au] MBGDOZCTEJQOJU-UHFFFAOYSA-N 0.000 description 1
- FFDNCLQDXZUPCF-UHFFFAOYSA-N [V].[Zn] Chemical compound [V].[Zn] FFDNCLQDXZUPCF-UHFFFAOYSA-N 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 description 1
- 229940010048 aluminum sulfate Drugs 0.000 description 1
- 238000004873 anchoring Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- GVPFVAHMJGGAJG-UHFFFAOYSA-L cobalt dichloride Chemical compound [Cl-].[Cl-].[Co+2] GVPFVAHMJGGAJG-UHFFFAOYSA-L 0.000 description 1
- UFMZWBIQTDUYBN-UHFFFAOYSA-N cobalt dinitrate Chemical compound [Co+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O UFMZWBIQTDUYBN-UHFFFAOYSA-N 0.000 description 1
- 229910001981 cobalt nitrate Inorganic materials 0.000 description 1
- 229910000361 cobalt sulfate Inorganic materials 0.000 description 1
- 229940044175 cobalt sulfate Drugs 0.000 description 1
- KTVIXTQDYHMGHF-UHFFFAOYSA-L cobalt(2+) sulfate Chemical compound [Co+2].[O-]S([O-])(=O)=O KTVIXTQDYHMGHF-UHFFFAOYSA-L 0.000 description 1
- 230000002860 competitive effect Effects 0.000 description 1
- XTVVROIMIGLXTD-UHFFFAOYSA-N copper(II) nitrate Chemical compound [Cu+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O XTVVROIMIGLXTD-UHFFFAOYSA-N 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 229940032950 ferric sulfate Drugs 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 229910052738 indium Inorganic materials 0.000 description 1
- APFVFJFRJDLVQX-UHFFFAOYSA-N indium atom Chemical compound [In] APFVFJFRJDLVQX-UHFFFAOYSA-N 0.000 description 1
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 description 1
- 235000002867 manganese chloride Nutrition 0.000 description 1
- 239000011565 manganese chloride Substances 0.000 description 1
- 229940099607 manganese chloride Drugs 0.000 description 1
- MIVBAHRSNUNMPP-UHFFFAOYSA-N manganese(2+);dinitrate Chemical compound [Mn+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O MIVBAHRSNUNMPP-UHFFFAOYSA-N 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- LGQLOGILCSXPEA-UHFFFAOYSA-L nickel sulfate Chemical compound [Ni+2].[O-]S([O-])(=O)=O LGQLOGILCSXPEA-UHFFFAOYSA-L 0.000 description 1
- 229940053662 nickel sulfate Drugs 0.000 description 1
- 229910000363 nickel(II) sulfate Inorganic materials 0.000 description 1
- SIWVEOZUMHYXCS-UHFFFAOYSA-N oxo(oxoyttriooxy)yttrium Chemical compound O=[Y]O[Y]=O SIWVEOZUMHYXCS-UHFFFAOYSA-N 0.000 description 1
- 238000006303 photolysis reaction Methods 0.000 description 1
- 230000015843 photosynthesis, light reaction Effects 0.000 description 1
- 238000006479 redox reaction Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 238000001878 scanning electron micrograph Methods 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- NWONKYPBYAMBJT-UHFFFAOYSA-L zinc sulfate Chemical compound [Zn+2].[O-]S([O-])(=O)=O NWONKYPBYAMBJT-UHFFFAOYSA-L 0.000 description 1
- 229910000368 zinc sulfate Inorganic materials 0.000 description 1
- 229960001763 zinc sulfate Drugs 0.000 description 1
Images
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/133—Renewable energy sources, e.g. sunlight
Landscapes
- Catalysts (AREA)
Abstract
The invention relates to the technical field of electrochemical catalysis, in particular to a noble metal monatomic catalyst based on a high-entropy effect and a preparation method thereof 3‑x V 2 M x (OH) 2 O 7 ·2H 2 And O, wherein M is an optional metal and is three or more of Ni, co, fe, cu, al and Mn, and the noble metal monoatomic species is one or more of Au, ru, in and Pt. Book (I)The noble metal monatomic composite catalyst prepared by the method has the advantages of regular shape, good crystallinity and adjustable types and proportions of metal elements of the high-entropy hydroxide substrate, can be used for preparing various noble metal monatomic catalysts, and has wide application prospect in the field of catalysis.
Description
Technical Field
The invention relates to the technical field of electrochemical catalysis, in particular to a noble metal monatomic catalyst based on a high entropy effect and a preparation method thereof.
Background
The energy is a foundation stone existing and developing in human society, is a basic restriction condition for economic development and civilization progress, and is an important basis for national economy and national security and realization of sustainable development. Under the guidance of the targets of 'carbon peak reaching and carbon neutralization', hydrogen energy is emerging as a recognized zero-carbon energy source after new energy sources such as solar energy, wind energy and the like are developed rapidly. The preparation technology of the hydrogen mainly comprises hydrogen production by fossil fuel, hydrogen production by water electrolysis, hydrogen production by water photolysis 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 as an energy source. However, water electrolysis is a complex redox reaction process involving multi-electron transfer between the positive electrode and the negative electrode, and therefore, the water electrolysis catalyst is one of the key factors for determining the cost of hydrogen production from water electrolysis.
Currently, the most widely used in industry is alkaline water electrolysis technology, under the current technical conditions, noble metals platinum and yttrium oxide/ruthenium oxide are respectively cathode and anode catalysts with higher catalytic efficiency, but the expensive price and poor stability severely limit the industrial application of the noble metals. Therefore, the electrolytic water catalyst for improving the utilization rate and the catalytic stability of the noble metal catalyst is the key of the competitive power of the technical core for large-scale popularization.
The high-entropy oxyhydroxide is a novel functional material which is derived and developed on the basis of high-entropy alloy, consists of oxygen ions, hydroxyl ions and five or more than five metal elements and has unique structure and function adjustable characteristic. In a highly disordered multicomponent system, the high-entropy oxyhydroxide has a series of unique characteristics, such as lattice distortion effect, high-entropy effect, delayed diffusion effect and cocktail effect, due to the larger mixing entropy.
In recent years, the monatomic composite material is used as a novel catalyst, noble metal atoms are anchored on a substrate, the atom utilization rate and the stability of the noble metal can be greatly improved, and the monatomic composite material has a unique electronic structure and excellent catalytic performance, and is a research hotspot in the field of catalysis. However, the noble metal monoatomic has very high surface free energy, so that it is easy to agglomerate to form clusters and nanoparticles, and thus the preparation of the monoatomic catalyst is a challenge; meanwhile, a large doping amount is easy to agglomerate to form clusters, but too low doping amount cannot ensure the number of catalytic active sites, which affects the activity of the monatomic catalyst to a certain extent. Therefore, the preparation method of noble metal monatomic catalyst with uniform size and rich catalytic active sites is still in the research and development stage.
Disclosure of Invention
The invention provides a noble metal monatomic catalyst based on a high entropy effect and a preparation method thereof, which can solve the problems of low loading capacity and uneven fraction of the monatomic catalyst in the prior art.
A noble metal monatomic catalyst based on high-entropy effect is a noble metal monatomic 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 And O, wherein M is an optional metal and is three or more of Ni, co, fe, cu, al and Mn, and the single atom species of the noble metal is one or more of Au, ru, in and Pt.
Preferably, each optional metal element is present in an atomic percentage of 0.05 to 0.3 of all non-noble metal elements.
A preparation method of a noble metal monatomic catalyst based on a high entropy effect specifically comprises the following steps:
step S1, adding vanadium pentoxide and inorganic non-noble metal salt into distilled water serving as a solvent, and performing ultrasonic mixing to obtain a mixed metal salt solution;
s2, under the condition of magnetic stirring, sequentially adding a mixed metal salt solution, a 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 the grey brown powder on the upper layer in the reaction kettle, centrifugally washing, and drying in vacuum to obtain the noble metal monatomic 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 vanadium ion concentration in the precursor solution in step S2 is 0.14 to 0.17 mol.L -1 The concentration of zinc ions is 0.03-0.05 mol.L -1 Sodium sulfate is 0.10-0.14 mol.L -1 The concentration of urotropin is 0.06-0.11 mol.L -1 The concentration of 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 。
Due to the adoption of the technical scheme, the invention has the remarkable technical effects that:
(1) The noble metal monatomic catalyst is a noble metal monatomic supported high-entropy oxyhydroxide catalyst, the substrate of the noble metal monatomic supported high-entropy oxyhydroxide catalyst is high-entropy oxyhydroxide, and based on the unique property of the high-entropy oxyhydroxide, the noble metal monatomic catalyst is an excellent electrolytic water catalyst on one hand, the activity of the catalyst can be improved to a certain extent, and meanwhile, the noble metal monatomic supported high-entropy oxyhydroxide catalyst can be used as an excellent carrier to anchor noble metal monatomic, so that the loading amount and the stability of the monatomic are improved.
(2) The substrate high-entropy hydroxide oxide has good crystallinity and regular shape, the types and the proportions of metal elements are adjustable, and the coordination environment of the monatomic catalyst can be changed by the cocktail effect of the high-entropy compound, so that the electronic structure of the monatomic catalyst is regulated, the electronic structure of the noble metal monatomic catalyst is regulated, the coordination environment of the catalyst is optimized, and the monatomic catalyst with multifunctional catalytic property is prepared.
(3) The types and the proportion of metal elements in the high-entropy oxyhydroxide are adjustable, and the special high-entropy effect can provide coordination environment and bonding action for anchoring different types of noble metal monoatomic atoms. Therefore, the invention provides a general monatomic catalyst synthesis strategy, and provides a new idea for the controllable preparation of the monatomic catalyst.
Drawings
FIG. 1 is a scanning electron micrograph of a monoatomic Ru-Au-Pt-in supported Zn-V-Al-Ni-Co-Fe-Cu-Mn oxyhydroxide prepared in example 1;
FIG. 2 is an X-ray powder diffraction pattern of a monoatomic Ru-Au-Pt-in-supported Zn-V-Al-Ni-Co-Fe-Cu-Mn-OH oxide prepared in example 1;
FIG. 3 is an X-ray energy spectrum of the monoatomic Ru-Au-Pt-in supported Zn-V-Al-Ni-Co-Fe-Cu-Mn oxyhydroxide prepared in example 1;
FIG. 4 is a high angle annular dark field transmission and energy spectrum profile of a single atom Ru-Au-Pt-in supported Zn-V-Al-Ni-Co-Fe-Cu-Mn-OH oxide prepared in example 1;
FIG. 5 is a transmission electron micrograph of single atom Ru-Au-Pt-in supported Zn-V-Al-Ni-Co-Fe-Cu-Mn-OH oxide prepared in example 1 corrected by spherical aberration;
FIG. 6 is an electrolytic water polarization curve for a monatomic Ru-Au-Pt-in supported Zn-V-Al-Ni-Co-Fe-Cu-Mn-OH oxide working electrode prepared in example 1;
FIG. 7 is an X-ray powder diffraction pattern of the monoatomic ruthenium indium supported zinc vanadium aluminum nickel cobalt iron oxyhydroxide prepared in example 2;
FIG. 8 is a transmission electron micrograph of the monoatomic platinum supported Zn-V-Al-Ni-Co-Fe-oxyhydroxide prepared in example 2 corrected for spherical aberration;
FIG. 9 is an X-ray powder diffraction pattern of a monatomic platinum-supported zinc vanadium nickel copper manganese oxyhydroxide prepared in example 3;
FIG. 10 is a transmission electron micrograph of the spherical aberration corrected zinc vanadium nickel copper manganese oxyhydroxide supported on monoatomic platinum prepared in example 3.
Detailed Description
For a further understanding of the present invention, reference is made to the following detailed description taken in conjunction with the accompanying drawings and examples. It is to be understood that the examples are illustrative of the invention and not limiting.
Example 1
The embodiment 1 of the invention relates to a noble metal monatomic catalyst based on a high-entropy stabilizing effect, in particular to a zinc-vanadium-aluminum-nickel-cobalt-iron-copper-manganese hydroxide catalyst loaded by monatomic ruthenium-gold-platinum-indium, and a preparation method of the catalyst 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 zinc ion concentration is 0.03 mol.L -1 And the concentration of aluminum ions is 0.01 mol.L -1 And the concentration of nickel ions is 0.01 mol.L -1 And the cobalt ion concentration is 0.01 mol.L -1 And the iron ion concentration is 0.01 mol.L -1 The copper ion concentration is 0.01 mol.L -1 The concentration of manganese ions was 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) On the basis of magnetic stirring, adding the mixed solution, chloroauric acid, ruthenium chloride, indium nitrate, chloroplatinic acid, urotropine and sodium sulfate reagents in the step (1) in sequence, wherein the adding time interval of each reagent is 5 minutes, after mixing, carrying out magnetic stirring for 30 minutes, and controlling the gold ion concentration in the precursor solution to be 0.001 mol.L -1 The concentration of ruthenium ions was 0.001 mol. L -1 And the indium ion concentration is 0.001 mol.L -1 The platinum ion concentration was 0.001 mol. L -1 The concentration of urotropin is 0.06 mol.L -1 Sodium sulfate concentration of 0.10 mol. L -1 Finally, ultrasonically treating the mixed solution stirred by the magnetic force for 60 minutes to ensure that the solution is uniformly mixed;
(3) And (3) transferring the mixed solution obtained in the step (2) into a reaction kettle, sealing the reaction kettle, carrying out hydrothermal reaction at 110 ℃ for 24 hours, cooling, collecting the grey brown powder on the upper layer in the reaction kettle, centrifugally washing, and drying to obtain the product, namely the monoatomic ruthenium-gold-platinum-indium loaded zinc-vanadium-aluminum-nickel-cobalt-iron-copper-manganese oxyhydroxide.
Referring to the attached drawings, fig. 1 is a scanning electron microscope image of the monatomic ruthenium gold platinum indium-loaded zinc vanadium aluminum nickel cobalt iron copper manganese oxyhydroxide prepared in the embodiment, and it can be known that the monatomic catalyst prepared in the embodiment has a nanosheet structure and a regular morphology, and no attachments such as obvious nanoparticles and the like are present on the surface of the nanosheet.
Fig. 2 and fig. 3 are an X-ray powder diffraction pattern and an X-ray energy spectrum of the monatomic ru-au-pt-in supported zn-v-al-ni-co-fe-cu-mn oxyhydroxide prepared in this example, all diffraction peaks in the X-ray powder diffraction pattern have a significant left shift relative to the standard card JCPDF NO #50-0750, and NO diffraction peaks of other impurities, respectively, and the X-ray energy spectrum proves that the prepared catalyst contains metallic elements of zn, v, al, ni, co, fe, cu, mn, ru, au, pt, and in. The ICP test is combined to prove that the noble metal single-atom catalyst synthesized by the embodiment 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 an energy spectrum scan of the monatomic ru-au-pt-in supported zinc-vanadium-aluminum-nickel-cobalt-iron-copper-manganese-oxyhydroxide prepared in this example, and the metal elements on the data surface are uniformly distributed on the nanosheets without obvious element aggregation and enrichment.
Fig. 5 is a transmission electron microscope image of spherical aberration correction of zinc vanadium aluminum nickel cobalt iron copper manganese oxyhydroxide loaded by monoatomic ruthenium gold platinum indium prepared in this example, and heavy metal elements ruthenium, gold, platinum, and indium on the data surface are dispersed on the zinc vanadium aluminum nickel cobalt iron copper manganese high-entropy oxyhydroxide nanosheets in a monoatomic manner.
Therefore, as can be seen from fig. 1, fig. 2, fig. 3, fig. 4 and fig. 5, we successfully prepared the monatomic ru-au-pt-in supported zinc-vanadium-aluminum-nickel-cobalt-iron-copper-manganese oxyhydroxide nanosheet material.
The prepared high-entropy oxyhydroxide is prepared into an oxygen evolution reaction working electrode, the polarization curve test result is shown in figure 5, and the test result in figure 5 shows that the catalytic activity of the crystal porous high-entropy zinc-vanadium-aluminum-nickel-cobalt-iron-ruthenium oxyhydroxide catalyst product is greatly improved compared with that of commercial ruthenium oxide, because the prepared high-entropy oxyhydroxide has higher specific surface area and abundant catalytic activity sites, and the electronic structure of the catalyst can be regulated and controlled by the cocktail effect of the high-entropy compound, so that the activity of the catalyst is finally improved.
Example 2
The same as example 1, except that the monatomic ruthenium indium supported zinc vanadium aluminum nickel cobalt iron oxyhydroxide catalyst material was prepared in this example as follows:
(1) Adding a proper amount of distilled water as a solvent into a container, sequentially adding vanadium pentoxide, zinc sulfate, aluminum sulfate, nickel sulfate, cobalt sulfate and ferric sulfate reagents, and controlling the concentration of vanadium ions in the solution to be 0.17 mol.L -1 The zinc ion concentration is 0.05 mol.L -1 And the aluminum ion concentration is 0.02 mol.L -1 The concentration of nickel ions is 0.02 mol.L -1 And the cobalt ion concentration is 0.02 mol.L -1 And 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) On the basis of magnetic stirring, the mixed solution in the step (1), ruthenium chloride, indium chloride, urotropine and sodium sulfate reagent are added in sequence, the adding time interval 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 And the indium ion concentration is 0.005 mol.L -1 The concentration of urotropin is 0.11 mol.L -1 The sodium sulfate concentration was 0.14 mol. L -1 Finally, ultrasonically treating the mixed solution stirred by the magnetic force for 60 minutes to ensure that the solution is uniformly mixed;
(3) And (3) transferring the mixed solution obtained in the step (2) into a reaction kettle, sealing the reaction kettle, carrying out hydrothermal reaction at 130 ℃ for 36 hours, cooling, collecting the grey brown powder on the upper layer in the reaction kettle, centrifugally washing, and drying to obtain the product, namely the monoatomic ruthenium-indium-loaded zinc-vanadium-aluminum-nickel-cobalt-iron oxyhydroxide.
Referring to the drawings, FIGS. 7 and 8 are respectively a monoatomic ruthenium-indium-supported zinc vanadium prepared in the present exampleThe X-ray powder diffraction pattern and the spherical aberration correction transmission electron micrograph of the aluminum-nickel-cobalt-iron oxyhydroxide show that all diffraction peaks in the X-ray powder diffraction pattern have obvious left shift relative to a standard card JCPDF NO #50-0750 and do not have diffraction peaks of other impurities. The ICP test and the spherical aberration correction transmission electron microscope image are combined at the same time, so that the precious metal monoatomic catalyst synthesized by the embodiment is RuIn @ Zn 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 same as example 1, except that the monatomic platinum-supported zinc vanadium aluminum nickel copper manganese hydroxide catalyst material was prepared as follows in this example:
(1) Adding a proper amount of distilled water as a solvent into a container, sequentially adding vanadium pentoxide, zinc chloride, ferric sulfate, copper chloride and manganese sulfate reagents, and controlling the concentration of vanadium ions in the solution to be 0.15 mol.L -1 And the zinc ion concentration is 0.04 mol.L -1 And an aluminum ion concentration of 0.018 mol. L -1 (iii) a nickel ion concentration of 0.018 mol. L -1 The copper ion concentration was 0.018 mol. L -1 Manganese ion concentration of 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) On the basis of magnetic stirring, the mixed solution in the step (1), chloroplatinic acid, urotropine and sodium sulfate reagent are added in sequence, the adding time interval of each reagent is 5 minutes, magnetic stirring is carried out for 30 minutes after mixing is finished, and the concentration of platinum ions in the precursor solution is controlled to be 0.004 mol.L -1 The concentration of urotropin is 0.1 mol.L -1 The sodium sulfate concentration was 0.13 mol. L -1 Finally, ultrasonically treating the mixed solution stirred by the magnetic force for 60 minutes to ensure that the solution is uniformly mixed;
(3) And (3) transferring the mixed solution obtained in the step (2) into a reaction kettle, sealing the reaction kettle, carrying out hydrothermal reaction at 120 ℃ for 30 hours, cooling, collecting the grey brown powder on the upper layer in the reaction kettle, centrifugally washing, and drying to obtain the product, namely the monatomic platinum-loaded zinc-vanadium-aluminum-nickel-copper-manganese oxyhydroxide.
Referring to the drawings, fig. 9 and 10 are an X-ray powder diffractogram and a spherical aberration correction transmission electron micrograph of the monoatomic platinum-supported zinc-vanadium-nickel-iron-manganese oxyhydroxide prepared in this example, respectively, in which all diffraction peaks in the X-ray powder diffractogram are significantly shifted to the left relative to standard card JCPDF NO #50-0750, and there are NO diffraction peaks of other impurities. The ICP test and the spherical aberration correction transmission electron microscope image are combined at the same time, so that the precious metal monoatomic catalyst synthesized by the embodiment is Pt @ Zn 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 same as example 1, except that the monatomic indium-platinum supported zinc vanadium iron copper manganese oxyhydroxide catalyst material was prepared in this example as follows:
(1) Adding a proper amount of distilled water as a solvent into a container, sequentially adding vanadium pentoxide, zinc chloride, ferric chloride, copper chloride and manganese chloride reagents, and controlling the concentration of vanadium ions in the solution to be 0.15 mol.L -1 The zinc ion concentration is 0.04 mol.L -1 The cobalt ion concentration was 0.015 mol. L -1 And the iron ion concentration is 0.015 mol.L -1 The copper ion concentration was 0.015 mol. L -1 The manganese ion concentration was 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) On the basis of magnetic stirring, adding the mixed solution in the step (1), indium sulfate, chloroplatinic acid, urotropine and sodium sulfate reagent in sequence, wherein the adding time interval of each reagent is 5 minutes, and after the mixing is finished, carrying out magnetic stirring for 30 minutes, and controlling the concentration of indium ions in the precursor solution to be 0.003 mol.L -1 And the platinum ion concentration is 0.003 mol.L -1 The concentration of urotropin is 0.09 mol.L -1 The sodium sulfate concentration was 0.12 mol. L -1 Finally, ultrasonically treating the mixed solution stirred by the 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, carrying out hydrothermal reaction for 30 hours at 120 ℃, cooling and collecting the grey brown color of the upper layer in the reaction kettleAnd (3) centrifuging and washing the powder, and drying to obtain a product, namely the zinc vanadium iron copper manganese hydroxide loaded by the monatomic indium platinum. The combination of XRD and ICP tests can prove that the noble metal monatomic catalyst synthesized by the embodiment 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 same as example 1, except that the preparation of the monatomic platinum-indium supported zinc vanadium aluminum nickel cobalt iron manganese oxyhydroxide catalyst material in this example was as follows:
(1) Adding a proper amount of distilled water as a solvent into a container, sequentially adding vanadium pentoxide, zinc nitrate, aluminum chloride, nickel nitrate, cobalt chloride, ferric nitrate and manganese sulfate reagents, and controlling the concentration of vanadium ions in the solution to be 0.16 mol.L -1 The zinc ion concentration is 0.04 mol.L -1 And the aluminum ion concentration is 0.013 mol.L -1 The nickel ion concentration was 0.013 mol. L -1 The cobalt ion concentration was 0.013 mol. L -1 And the iron ion concentration is 0.013 mol.L -1 The manganese ion concentration was 0.013 mol. L -1 Carrying out ultrasonic treatment on the mixed solution for 30 minutes to ensure that the solution is uniformly mixed;
(2) On the basis of magnetic stirring, adding the mixed solution, chloroauric acid, indium sulfate, chloroplatinic acid, urotropine and sodium sulfate reagent in the step (1) in sequence, wherein the adding time interval of each reagent is 5 minutes, and after mixing, carrying out magnetic stirring for 30 minutes, and controlling the gold ion concentration in the precursor solution to be 0.002 mol.L -1 And the indium ion concentration is 0.002 mol.L -1 The platinum ion concentration was 0.002 mol. L -1 The concentration of urotropin is 0.1 mol.L -1 The sodium sulfate concentration was 0.12 mol. L -1 Finally, ultrasonically treating the mixed solution stirred by the 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, carrying out hydrothermal reaction at 120 ℃ for 28 hours, cooling, collecting the grayish brown powder on the upper layer in the reaction kettle, centrifugally washing, and drying to obtain a product, namely the monoatomic gold-platinum-indium-loaded zinc-vanadium-aluminum-nickel-cobalt-iron-manganese oxyhydroxide. The combination of XRD and ICP tests proves that the noble metal monatomic 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 present invention and its embodiments have been described above schematically, and the description is not intended to be limiting, and what is shown in the drawings is only one of the embodiments of the present invention, and the actual structure is not limited thereto. Therefore, without departing from the spirit of the present invention, a person of ordinary skill in the art should understand that the present invention shall not be limited to the embodiments and the similar structural modes without creative design.
Claims (8)
1. A noble metal monatomic catalyst based on the high entropy effect is characterized in that: the 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 And O, wherein M is an optional metal and is three or more of Ni, co, fe, cu, al and Mn, and the noble metal monoatomic species is one or more of Au, ru, in and Pt.
2. A noble metal monatomic catalyst based on the high entropy effect according to claim 1, characterized in that: each optional metal element accounts for 0.05-0.3 atomic percent of all non-noble metal elements.
3. A preparation method of a noble metal monatomic catalyst based on a high entropy effect is characterized by comprising 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;
s2, under the condition of magnetic stirring, 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 the grey brown powder on the upper layer in the reaction kettle, centrifugally washing, and drying in vacuum to obtain the noble metal monatomic catalyst.
4. A process for the preparation of a noble metal monatomic catalyst based on a high entropy effect according to claim 3, characterized in that: in the step S1, the inorganic non-noble metal salt is nitrate, sulfate and/or hydrochloride.
5. A process for the preparation of a noble metal monatomic catalyst based on a 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.
6. The preparation method of the noble metal monatomic catalyst based on the 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.
7. The preparation method of the noble metal monatomic catalyst based on the 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.
8. The preparation method of the noble metal monatomic catalyst based on the high entropy effect according to claim 3, characterized in that: the concentration of vanadium ions in the precursor solution in the step S2 is 0.14-0.17 mol.L -1 The concentration of zinc ions is 0.03-0.05 mol.L -1 Sodium sulfate is 0.10-0.14 mol.L -1 The concentration of urotropin is 0.06-0.11 mol.L -1 The concentration of inorganic non-noble metal 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 。
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202211479510.2A CN115896810B (en) | 2022-11-24 | 2022-11-24 | Noble metal monoatomic catalyst based on high entropy effect and preparation method thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202211479510.2A CN115896810B (en) | 2022-11-24 | 2022-11-24 | Noble metal monoatomic catalyst based on high entropy effect and preparation method thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
CN115896810A true CN115896810A (en) | 2023-04-04 |
CN115896810B CN115896810B (en) | 2023-12-01 |
Family
ID=86480097
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202211479510.2A Active CN115896810B (en) | 2022-11-24 | 2022-11-24 | Noble metal monoatomic catalyst based on high entropy effect and preparation method thereof |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN115896810B (en) |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2021128282A1 (en) * | 2019-12-27 | 2021-07-01 | 江南大学 | Iron-cobalt-nickel-copper-based high-entropy alloy water electrolysis catalytic material and preparation method therefor |
CN113224324A (en) * | 2021-07-08 | 2021-08-06 | 成都大学 | Palladium-doped aluminum-cobalt-chromium-iron-nickel high-entropy alloy composite electrode and preparation method thereof |
CN113522308A (en) * | 2021-07-14 | 2021-10-22 | 中国地质大学(武汉) | High-entropy alloy catalyst and preparation method and application thereof |
CN114420953A (en) * | 2021-12-29 | 2022-04-29 | 浙江大学 | Preparation method of silver/high-entropy hydroxide oxide nano composite material |
WO2022143265A1 (en) * | 2020-12-31 | 2022-07-07 | 北京单原子催化科技有限公司 | Noble metal single atom supported three-way catalyst and preparation method therefor and use thereof |
US20220234908A1 (en) * | 2021-01-28 | 2022-07-28 | Zhejiang University | A-site high-entropy nanometer metal oxide with high conductivity, and preparation method thereof |
CN114808123A (en) * | 2022-04-18 | 2022-07-29 | 东莞理工学院 | Single-crystal porous high-entropy oxyhydroxide and preparation method and application thereof |
CN115044935A (en) * | 2022-07-29 | 2022-09-13 | 东北大学秦皇岛分校 | Preparation method and application of nano high-entropy oxide |
CN115159590A (en) * | 2022-07-21 | 2022-10-11 | 江苏电子信息职业学院 | High-entropy transition metal oxyhydroxide and preparation method and application thereof |
-
2022
- 2022-11-24 CN CN202211479510.2A patent/CN115896810B/en active Active
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2021128282A1 (en) * | 2019-12-27 | 2021-07-01 | 江南大学 | Iron-cobalt-nickel-copper-based high-entropy alloy water electrolysis catalytic material and preparation method therefor |
WO2022143265A1 (en) * | 2020-12-31 | 2022-07-07 | 北京单原子催化科技有限公司 | Noble metal single atom supported three-way catalyst and preparation method therefor and use thereof |
US20220234908A1 (en) * | 2021-01-28 | 2022-07-28 | Zhejiang University | A-site high-entropy nanometer metal oxide with high conductivity, and preparation method thereof |
CN113224324A (en) * | 2021-07-08 | 2021-08-06 | 成都大学 | Palladium-doped aluminum-cobalt-chromium-iron-nickel high-entropy alloy composite electrode and preparation method thereof |
CN113522308A (en) * | 2021-07-14 | 2021-10-22 | 中国地质大学(武汉) | High-entropy alloy catalyst and preparation method and application thereof |
CN114420953A (en) * | 2021-12-29 | 2022-04-29 | 浙江大学 | Preparation method of silver/high-entropy hydroxide oxide nano composite material |
CN114808123A (en) * | 2022-04-18 | 2022-07-29 | 东莞理工学院 | Single-crystal porous high-entropy oxyhydroxide and preparation method and application thereof |
CN115159590A (en) * | 2022-07-21 | 2022-10-11 | 江苏电子信息职业学院 | High-entropy transition metal oxyhydroxide and preparation method and application thereof |
CN115044935A (en) * | 2022-07-29 | 2022-09-13 | 东北大学秦皇岛分校 | Preparation method and application of nano high-entropy oxide |
Non-Patent Citations (4)
Title |
---|
HAITAO XU等: "Electronic Interaction between In Situ Formed RuO2 Clusters and a Nanoporous Zn3V3O8 Support and Its Use in the Oxygen Evolution Reaction", ACS APPLIED MATERIALS & INTERFACES, vol. 13, pages 54951 - 54958 * |
LINGJIE ZHANG等: "Implanting an Electron Donor to Enlarge the d-p Hybridization of High-Entropy (Oxy)hydroxide:A Novel Design to Boost Oxygen Evolution", ADVANCED MATERIALS, vol. 34, no. 26, pages 2110511 * |
姚宏伟;卢一平;曹志强;王同敏;李廷举;: "FCC/L1_2共格高熵高温合金的研究进展", 材料导报, vol. 34, no. 17, pages 17041 - 17046 * |
许海涛等: "动态预压缩对 CoCrFeNiMn 高熵合金微尺度压入硬度的影响", 高压物理学报, vol. 35, no. 6, pages 064101 * |
Also Published As
Publication number | Publication date |
---|---|
CN115896810B (en) | 2023-12-01 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN114808123B (en) | Single crystal porous high entropy hydroxyl oxide and preparation method and application thereof | |
CN111450851B (en) | Preparation method of sulfur-doped cobalt-based nano oxygen evolution electrocatalyst | |
CN111530474A (en) | Noble metal monoatomic regulation spinel array catalyst and preparation method and application thereof | |
CN112490451A (en) | Cu-CoNCNs catalyst derived from folic acid, preparation and application thereof | |
CN108842165B (en) | Solvothermal preparation of sulfur doped NiFe (CN)5NO electrolysis water oxygen evolution catalyst and application thereof | |
CN111640953A (en) | Air electrode catalyst of aluminum-air battery and preparation method thereof | |
CN114990612B (en) | Indium-based perovskite catalyst LaInO 3 Is prepared from (1) and its application | |
CN114892206B (en) | Multi-metal nitride heterojunction nanorod array composite electrocatalyst and preparation method and application thereof | |
CN115896810B (en) | Noble metal monoatomic catalyst based on high entropy effect and preparation method thereof | |
CN115161691A (en) | Oxygen evolution catalyst of FeCoNiMg high-entropy amorphous alloy powder and preparation method thereof | |
CN113293407B (en) | Iron-rich nanobelt oxygen evolution electrocatalyst and preparation method thereof | |
CN111394748A (en) | For CO2Electrolytic iron-nickel alloy in-situ desolventizing layered perovskite cathode material | |
CN114649538B (en) | Electro-catalyst for preparing hydrogen by methanol electrolysis and preparation method thereof | |
CN114717599B (en) | Ruthenium-supported nickel metal three-dimensional carbon sphere electrocatalyst and preparation method and application thereof | |
CN114622240B (en) | General preactivation method of anti-perovskite nitride, and product and application thereof | |
CN113955728B (en) | Preparation of cobalt phosphide/cobalt manganese phosphide with hollow grade structure and application of electrolytic water | |
CN116949502A (en) | Nickel-iron layered hydroxide electrolyzed water catalyst with low platinum load, and preparation method and application thereof | |
CN118016908A (en) | Preparation method and application of Ce-doped Ni-based electrocatalyst | |
CN117604570A (en) | Ru doped SrFeO 3-δ Three-functional perovskite electrocatalytic material and preparation method and application thereof | |
CN117926339A (en) | Platinum-based composite catalyst for alkaline electrolyzed water and preparation method thereof | |
CN117604556A (en) | Preparation method and application of double-phase composite anode catalyst for seawater electrolysis hydrogen production | |
CN115522216A (en) | Phosphorus-doped pentlandite electrocatalyst and preparation method thereof | |
CN118127554A (en) | Carbon fiber cloth supported transition metal catalyst and preparation method and application thereof | |
CN116463662A (en) | Oxygen evolution electrode and preparation method and application thereof | |
CN117448878A (en) | Nickel-based ferromolybdenum diatomic integral electrode and preparation method and application thereof |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |