CN106807349A - A kind of nano metal simple substance modification transition metal hydroxide array catalyst and its preparation method and application - Google Patents

A kind of nano metal simple substance modification transition metal hydroxide array catalyst and its preparation method and application Download PDF

Info

Publication number
CN106807349A
CN106807349A CN201710060056.XA CN201710060056A CN106807349A CN 106807349 A CN106807349 A CN 106807349A CN 201710060056 A CN201710060056 A CN 201710060056A CN 106807349 A CN106807349 A CN 106807349A
Authority
CN
China
Prior art keywords
transition metal
metal hydroxide
simple substance
preparation
nano
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
CN201710060056.XA
Other languages
Chinese (zh)
Inventor
杨秀荣
邢志财
孙健
黄建设
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.)
Changchun Institute of Applied Chemistry of CAS
Original Assignee
Changchun Institute of Applied Chemistry of CAS
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 Changchun Institute of Applied Chemistry of CAS filed Critical Changchun Institute of Applied Chemistry of CAS
Priority to CN201710060056.XA priority Critical patent/CN106807349A/en
Publication of CN106807349A publication Critical patent/CN106807349A/en
Pending legal-status Critical Current

Links

Classifications

    • 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
    • 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
    • B01J23/002Mixed oxides other than spinels, e.g. perovskite
    • 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
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/74Iron group metals
    • B01J23/75Cobalt
    • 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
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/74Iron group metals
    • B01J23/755Nickel
    • 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
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/89Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
    • B01J23/8913Cobalt and noble metals
    • 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
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • C02F1/46109Electrodes
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • C02F1/4618Devices therefor; Their operating or servicing for producing "ionised" acidic or basic water
    • 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
    • C25B11/051Electrodes formed of electrocatalysts on a substrate or carrier
    • 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
    • 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
    • C25B11/081Electrodes formed of electrocatalysts on a substrate or carrier characterised by the electrocatalyst material consisting of a single catalytic element or catalytic compound the element being a noble metal
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • C02F1/46109Electrodes
    • C02F2001/46133Electrodes characterised by the material
    • C02F2001/46138Electrodes comprising a substrate and a coating
    • C02F2001/46142Catalytic coating
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Electrochemistry (AREA)
  • Metallurgy (AREA)
  • General Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Inorganic Chemistry (AREA)
  • Catalysts (AREA)
  • Electrodes For Compound Or Non-Metal Manufacture (AREA)

Abstract

The present invention provides a kind of nano metal simple substance modification transition metal hydroxide array catalyst and its preparation method and application, belongs to alkalescence and Neutral Electrolysis water decomposes field.The catalyst first prepares transition metal hydroxide array, and be then respectively working electrode and electrolyte with above-mentioned transition metal hydroxide array and the second metal salt solution prepares nano metal simple substance modification transition metal hydroxide array by electro-deposition techniques.The present invention also provides the nano metal simple substance modification transition metal hydroxide array catalyst that above-mentioned preparation method is obtained.Preparation-obtained nano metal simple substance modification transition metal hydroxide array catalyst is applied in alkalescence and Neutral Electrolysis pond, with excellent electrocatalytic hydrogen evolution performance and full electrolysis water performance.

Description

A kind of nano metal simple substance modifies transition metal hydroxide array catalyst and its system Preparation Method and application
Technical field
Field is decomposed the present invention relates to alkalescence and Neutral Electrolysis water, and in particular to a kind of nano metal simple substance modifies transition Metal hydroxides array catalyst and its preparation method and application.
Background technology
Energy crisis and environmental pollution are 21 century two very severe problems facing of the whole world.In recent years, with stone The increasingly exhaustion of the non-renewable fossil energy such as oil and coal, simultaneous carbon dioxide largely produces that is triggered " to imitate in greenhouse Should " increasingly sharpen, countries in the world have all turned to the center of gravity of research the research and development of new energy.Persistence grinds in market Study carefully company to claim, as national governments tend to more strict to the pay attention to day by day fuel specification of environmental protection, by gasoline in global range and Diesel oil reduction sulfur content requirement drive, global hydrogen demand will increase by 27% before the year two thousand twenty, from 2013 when 255,300,000,000 cubes Rice increases to 3248 billion cubic meters during the year two thousand twenty.Hydrogen is in oil refining, chemical industry, float glass, metal material and food production etc. The consumption rapid growth in field.The nations of China and India will be promoted to implement stricter in road fuel field the need for clean air Regulation, so as to make the Asian-Pacific area turn into the maximum hydrogen market in the whole world.In North America, road fuel specifies or will be further strict, This will need to produce the gasoline and diesel oil of ultralow sulfur-bearing.Therefore, how to realize that preparation of industrialization hydrogen enjoys vast research work The concern of person.
The method for commonly using natural gas pyrolysis reformation at present prepares hydrogen, thus inevitably a large amount of useizations Stone fuel and emission greenhouse gas, it is impossible to realize real " green clean manufacturing ".And utilize renewable wind energy, solar energy etc. Hydrogen prepared by the energy such as is subject to energy intermittence, is difficult to store and transport limited at the inferior position.And water electrolysis hydrogen production is to realize work Industry, the cheap important means for preparing hydrogen.Recently, researcher is to based on the abundant and cheap metal sulfide of the earth [Science 2007,317,100;Nat.Mater.2012,11,963;Nat.Mater.2013,12,850;Energy Environ.Sci.2014,7,3519;Energy Environ.Sci.2013,6,3553], nitride [Angew.Chem., Int.Ed.2012,51,6131], boride [Angew.Chem., Int.Ed.2012,51,12703] and phosphide The liberation of hydrogen such as [J.Am.Chem.Soc.2013,135,9267] catalyst has carried out numerous studies.However, exploitation design can be relatively low With the new catalyst of high reaction rate liberation of hydrogen under overpotential, and further improve its long-time stability and realize extensive decomposition Water hydrogen manufacturing is particularly important.
Recently, Xi'an Communications University Yang Bai human relations seminar reports low content platinum (5%) modification transition metal carbide and uses The research [Chem.Commun.2016,52,369716] of Hydrogen Evolution Performance under its alkalescence condition is improved.The Dalian Chemistry and Physics Institute bag letter and Seminar has delivered monoatomic metal modification molybdenum sulfide and can excite the paper of Hydrogen Evolution Performance under its acid condition, and the research is exploitation Two-dimensional material catalyst opens a frontier [Energy Environ.Sci.2015,8,1594].Additionally, array is catalyzed Agent has to be included good electric conductivity and structural stability is high, high surface contributes to active material efficient utilization and reduces to urge Advantage [the J.Am.Chem.Soc.2014,136,10053 such as chemical property are improved while agent consumption; Adv.Mater.2015,27,7051].Therefore, to improve catalyst catalytic performance and long-time stability, exploitation design is based on receiving The high-performance liberation of hydrogen catalyst of rice metal simple-substance modification transition metal hydroxide array electrode has huge challenge.
The content of the invention
The present invention provides one kind and receives to solve low and stability relative mistake the technical problem of existing catalyst activity Rice metal simple-substance modification transition metal hydroxide array catalyst and its preparation method and application.
The present invention provides the preparation method that a kind of nano metal simple substance modifies transition metal hydroxide array catalyst, should Method includes:
Step one:Prepare transition metal hydroxide array;
Step 2:Work electricity is respectively with gained transition metal hydroxide array and the second metal salt solution in step one Pole and electrolyte prepare nano metal simple substance and modify transition metal hydroxide array catalyst by electro-deposition techniques.
Preferably, described transition metal hydroxide array passes through hydro-thermal method, solvent-thermal method, chemical deposition or electricity It is prepared by sedimentation.
Preferably, described electrodeposition process be using conductive substrates and the first metal salt solution as working electrode and What electrolyte was prepared.
Preferably, the slaine in first metal salt solution is in nitrate, the chloride of iron, cobalt or nickel Kind.
Preferably, described conductive substrates are carbon cloth, nickel screen, copper mesh, titanium net or titanium sheet.
Preferably, described electrodeposition temperature is 25 DEG C;Electrodeposition time is 2~60 minutes.
Preferably, the slaine in second metal salt solution be cobalt chloride, nickel nitrate, cobaltous sulfate, ferrous sulfate, Nickel sulfate or chloroplatinic acid.
Preferably, the electrodeposition temperature of described step two is 25-30 DEG C;Electrodeposition time is 2~60 minutes.
The present invention also provides the nano metal simple substance modification transition metal hydroxide array that above-mentioned preparation method obtains and urges Agent.
The present invention also provide above-mentioned nano metal simple substance modification transition metal hydroxide array catalyst alkalescence and in Application in terms of property electrolytic cell.
Beneficial effects of the present invention
The present invention provides a kind of nano metal simple substance modification transition metal hydroxide array catalyst and preparation method thereof And application, the catalyst is first to prepare transition metal hydroxide array;Then by gained transition metal hydroxide array and Second metal salt solution is respectively working electrode and electrolyte and prepares nano metal simple substance modification transition gold by electro-deposition techniques Category hydroxide array catalyst.Above-mentioned preparation method is simple, can be mass-produced, preparation-obtained array catalyst application In alkalescence and Neutral Electrolysis pond, with excellent electrocatalytic hydrogen evolution and full electrolysis water performance.
Brief description of the drawings
Fig. 1 is the surface sweeping electromicroscopic photograph figure that the platinum that embodiment 1 is prepared modifies cobalt hydroxide nano-chip arrays;
Fig. 2 is the transmission electron microscope picture that the platinum that embodiment 1 is prepared modifies cobalt hydroxide nano-chip arrays;
Fig. 3 is that the platinum that embodiment 1 is prepared modifies cobalt hydroxide nano-chip arrays polarization curve in the basic conditions Figure;
Fig. 4 is that the platinum that embodiment 1 is prepared modifies cobalt hydroxide nano-chip arrays polarization curve in neutral conditions Figure;
Fig. 5 is the stereoscan photograph figure that the nickel that embodiment 2 is prepared modifies nickel hydroxide nano chip arrays;
Fig. 6 is that the nickel that embodiment 2 is prepared modifies nickel hydroxide nano chip arrays polarization curve in the basic conditions Figure;
Fig. 7 is that the nickel that embodiment 2 is prepared modifies nickel hydroxide nano chip arrays in two electrode system neutral and alkali conditions Under polarization curve.
Specific embodiment
The present invention provides the preparation method that a kind of nano metal simple substance modifies transition metal hydroxide array catalyst, should Method includes:
Step one:Prepare transition metal hydroxide array;
Step 2:Work electricity is respectively with gained transition metal hydroxide array and the second metal salt solution in step one Pole and electrolyte prepare nano metal simple substance and modify transition metal hydroxide array catalyst by electro-deposition techniques.
According to the present invention, transition metal hydroxide array is first prepared, the system of described transition metal hydroxide array Preparation Method is not particularly limited, using hydro-thermal method well known to those skilled in the art, solvent-thermal method, chemical deposition or electro-deposition Method, preferably hydro-thermal method or electrodeposition process.
First metal salt solution is preferably dissolved in solvent and fully dissolved by described hydro-thermal method in a kettle., then by conduction Substrate cleans the intercalation reaction kettle that retreads with watery hydrochloric acid, ethanol, deionization;It is put into after sealed reactor in convection oven in 100- 8 hours are reacted at 180 DEG C;Transition metal hydroxide is obtained after being rinsed repeatedly with ethanol and deionized water after natural cooling Array.Slaine in the first described metal salt solution is preferably the one kind in the nitrate of iron, cobalt or nickel, chloride, more Preferably cobalt nitrate, nickel nitrate, ferrous sulfate or nickel sulfate;Solvent is preferably hexamethylenetetramine;Described conductive substrates are excellent Elect the substrates such as carbon cloth, nickel screen, copper mesh, titanium net or titanium sheet as.
Described electro-deposition method is preferably with conductive substrates as working electrode, graphite flake is to be to electrode, silver/silver chlorate Electro-deposition is carried out using CHI660E types electrochemical workstation in the three-electrode system of reference electrode, electrolyte is the first slaine Solution is molten, and electrodeposition temperature is preferably 25 DEG C, and sedimentation time is 2~60 minutes, more preferably 5~15 minutes, will be post-depositional Sample can obtain transition metal hydroxide array after being washed with deionized water and ethanol.The first described slaine is molten Slaine in liquid is preferably the one kind in the nitrate of iron, cobalt or nickel, chloride, more preferably cobalt nitrate, ferrous sulfate or Nickel sulfate;Described conductive substrates are preferably the substrates such as carbon cloth, nickel screen, copper mesh, titanium net or titanium sheet.
According to the present invention, by above-mentioned gained transition metal hydroxide array be working electrode, graphite flake be to electrode, To carry out electro-deposition using CHI660E types electrochemical workstation in the three-electrode system of reference electrode, electrolyte is silver/silver chlorate Second metal salt solution, electrodeposition temperature is preferably 25-30 DEG C, and sedimentation time is 2~60 minutes, more preferably 5~15 minutes, The method of described electro-deposition is preferably cyclic voltammetry, and electricity volt is preferably -0.2~-1.4 volts, post-depositional sample is passed through Nano metal simple substance modification transition metal hydroxide array catalyst is can obtain after being washed with deionized water and ethanol.It is described Slaine in second metal salt solution is preferably cobalt chloride, nickel nitrate, cobaltous sulfate, ferrous sulfate, nickel sulfate or chloroplatinic acid.
The present invention nano metal simple substance modification transition metal hydroxide array that also the offer above method is prepared is urged Agent.
The present invention also provide above-mentioned nano metal simple substance modification transition metal hydroxide array catalyst alkalescence and in Property electrolytic cell in terms of application, using above-mentioned nano metal simple substance modify transition metal hydroxide array as negative electrode, anode or Battery is helped in negative and positive level assembling, using CHI660E type electrochemical workstations test its electrocatalytic hydrogen evolution in alkaline electrolyte, Analysis oxygen performance.
With reference to embodiment, the present invention will be further described in detail, and the raw material being related in embodiment is commercially available Obtain.
Embodiment 1
1.45 grams of cobalt nitrates are weighed respectively and 1.4 grams of hexamethylenetetramines are dissolved in 35 ml deionized waters, treat that it fills 50 milliliters of reactors are transferred to after dividing dissolving;Carbon cloth is cleaned into the intercalation reaction kettle that retreads with watery hydrochloric acid, ethanol, deionization;Sealing It is put into after reactor in convection oven and reacts 8 hours at 100 DEG C;After being rinsed repeatedly with ethanol and deionized water after natural cooling Obtain cobalt hydroxide nano-chip arrays.
It is to use pole CHI660E type electrochemistry using above-mentioned cobalt hydroxide nano-chip arrays as working electrode, graphite flake Work station carries out platinum electro-deposition, and electrolyte is the mixing of 1 mmoles chloroplatinic acid, 0.5 mmoles sodium hypophosphite and 0.2 mmoles sodium citrate Solution, 3.5 are adjusted to using NaOH by pH, then with 0.25 milliampere/centimetre2Current density electro-deposition 15 at 30 DEG C Minute, platinum modification cobalt hydroxide nano-chip arrays are obtained after being rinsed repeatedly using ethanol and deionized water.
Fig. 1 is the surface sweeping electromicroscopic photograph figure that the platinum that embodiment 1 is prepared modifies cobalt hydroxide nano-chip arrays, wherein scheming A is the stereoscan photograph under 5 microns of scales, and figure b is the stereoscan photograph under 500 m-ns, the figure illustrates carbon cloth It is completely covered by nano-chip arrays, its length is about 0.5~2 micron, and thickness is 10~30 nanometers.Fig. 2 is prepared into for embodiment 1 The platinum for arriving modifies the transmission electron microscope photo figure of cobalt hydroxide nano-chip arrays, wherein figure a is the transmission electron microscope under 200 m-ns Photo, figure b is the transmission electron microscope photo under 5 m-ns, and the figure shows can just see diameter about 2~4 only in high-resolution The Pt nanoparticle (Fig. 2 b) of nanometer.Fig. 3 shows the catalyst (1 rub potassium hydroxide, pH=14) pole in the basic conditions Change curve map.With compare cobalt hydroxide array compared with, increased considerably by catalytic performance after platinum electrodeposition, and with and business Change platinum carbon equally close to zero take-off potential, it is only necessary to 32 and 122 millivolts of overpotentials can drive 10 and 100 milliamperes/centimetre2Electricity Current density.Fig. 4 shows the catalyst (1 rub phosphate buffer, pH=7) polarization curve in neutral conditions.With it is right Compared according to cobalt hydroxide array, the catalyst equally illustrates excellent catalytic performance in neutral conditions.
Embodiment 2
With carbon cloth as working electrode, graphite flake be three electrodes to electrode and silver/silver chlorate (3M KCl) as reference electrode Electro-deposition is carried out in system.Electrolyte rubs nickel nitrate solution for 0.1.Using CHI660E types electrochemical workstation with relative to full Deposited 7 minutes at 25 DEG C with the constant potential that calomel electrode (SCE) is 1 volt, hydrogen-oxygen is can obtain after second alcohol and water is cleaned Change nickel nano film array.
With nickel hydroxide nano chip arrays as working electrode, silver/silver chlorate is as reference electrode and 0.1 rubs nickel sulfate to be electrolysed Liquid, is deposited 15 minutes using cyclic voltammetry between -0.2~-1.4 volts, and elemental nickel is can obtain after second alcohol and water is cleaned The nickel hydroxide nano chip arrays of modification.
Fig. 5 is the surface sweeping electromicroscopic photograph figure that the nickel that embodiment 2 is prepared modifies nickel hydroxide nano chip arrays, wherein scheming A is the stereoscan photograph under 5 microns of scales, and figure b is the stereoscan photograph under 500 m-ns, the figure illustrates carbon cloth It is completely covered by nano-chip arrays, its length is about 30~100 nanometers, and thickness is 5~20 nanometers.Fig. 6 shows the catalyst (1 rub potassium hydroxide, pH=14) polarization curve in the basic conditions.Compared with nickel hydroxide array is compareed, electric deposition nickel Rear catalyst catalytic performance is significantly improved, and with the take-off potential as commercialization platinum carbon close to zero, needs 68 and 190 millivolts of mistakes Current potential can drive 10 and 100 milliamperes/centimetre2Current density.Fig. 7 is the nickel modification nickel hydroxide that embodiment 2 is prepared Polarization curve of the nano-chip arrays under the conditions of two electrode system neutral and alkalis, when current density is 10 milliamperes/centimetre2When nickel repair Current potential when decorations nickel hydroxide nano chip arrays catalyst electrode is relative to standard hydrogen electrode is 1.58 volts.
Embodiment 3
Cobalt hydroxide nano-chip arrays will be obtained in embodiment 1 for working electrode, graphite flake are to be to pole, silver/silver chlorate Reference electrode and 0.1 rubs nickel nitrate solution for electrolyte, is deposited 10 minutes between -0.2~-1.4 volts using cyclic voltammetry, leads to The cobalt hydroxide nano-chip arrays that elemental nickel is modified are can obtain after crossing the cleaning of second alcohol and water.
The nickel modification cobalt hydroxide nano-chip arrays that embodiment 3 is obtained carry out alkaline Hydrogen Evolution Performance test, need 163 millivolts Overpotential can drive 10 milliamperes/centimetre2Current density.
Embodiment 4
Cobalt hydroxide nano-chip arrays will be obtained in embodiment 1 for working electrode, graphite flake are to be to pole, silver/silver chlorate Reference electrode and 0.1 rubs copperas solution for electrolyte, is deposited 5 minutes between -0.2~-1.4 volts using cyclic voltammetry, The cobalt hydroxide nano-chip arrays that fe is modified are can obtain after second alcohol and water is cleaned.
The iron modification cobalt hydroxide nano-chip arrays that embodiment 4 is obtained carry out alkaline Hydrogen Evolution Performance test, need 215 millivolts Overpotential can drive 10 milliamperes/centimetre2Current density.

Claims (10)

1. a kind of nano metal simple substance modifies the preparation method of transition metal hydroxide array catalyst, it is characterised in that should Method includes:
Step one:Prepare transition metal hydroxide array;
Step 2:With in step one gained transition metal hydroxide array and the second metal salt solution be respectively working electrode and Electrolyte prepares nano metal simple substance and modifies transition metal hydroxide array catalyst by electro-deposition techniques.
2. a kind of nano metal simple substance according to claim 1 modifies the preparation of transition metal hydroxide array catalyst Method, it is characterised in that described transition metal hydroxide array passes through hydro-thermal method, solvent-thermal method, chemical deposition or electricity It is prepared by sedimentation.
3. a kind of nano metal simple substance according to claim 2 modifies the preparation of transition metal hydroxide array catalyst Method, it is characterised in that described electrodeposition process be using conductive substrates and the first metal salt solution as working electrode and What electrolyte was prepared.
4. a kind of nano metal simple substance according to claim 3 modifies the preparation of transition metal hydroxide array catalyst Method, it is characterised in that the slaine in first metal salt solution is in nitrate, the chloride of iron, cobalt or nickel Kind.
5. a kind of nano metal simple substance according to claim 3 modifies the preparation of transition metal hydroxide array catalyst Method, it is characterised in that described conductive substrates are carbon cloth, nickel screen, copper mesh, titanium net or titanium sheet.
6. a kind of nano metal simple substance according to claim 2 modifies the preparation of transition metal hydroxide array catalyst Method, it is characterised in that described electrodeposition temperature is 25 DEG C;Electrodeposition time is 2~60 minutes.
7. a kind of nano metal simple substance according to claim 1 modifies the preparation of transition metal hydroxide array catalyst Method, it is characterised in that slaine in second metal salt solution is cobalt chloride, nickel nitrate, cobaltous sulfate, ferrous sulfate, Nickel sulfate or chloroplatinic acid.
8. a kind of nano metal simple substance according to claim 1 modifies the preparation of transition metal hydroxide array catalyst Method, it is characterised in that the electrodeposition temperature of described step two is 25-30 DEG C;Electrodeposition time is 2~60 minutes.
9. the nano metal simple substance modification transition metal hydroxide that the preparation method described in claim 1-8 any one is obtained Array catalyst.
10. the nano metal simple substance modification transition metal hydroxide array catalyst described in claim 9 is in alkalescence and neutrality Application in terms of electrolytic cell.
CN201710060056.XA 2017-01-24 2017-01-24 A kind of nano metal simple substance modification transition metal hydroxide array catalyst and its preparation method and application Pending CN106807349A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710060056.XA CN106807349A (en) 2017-01-24 2017-01-24 A kind of nano metal simple substance modification transition metal hydroxide array catalyst and its preparation method and application

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710060056.XA CN106807349A (en) 2017-01-24 2017-01-24 A kind of nano metal simple substance modification transition metal hydroxide array catalyst and its preparation method and application

Publications (1)

Publication Number Publication Date
CN106807349A true CN106807349A (en) 2017-06-09

Family

ID=59112197

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710060056.XA Pending CN106807349A (en) 2017-01-24 2017-01-24 A kind of nano metal simple substance modification transition metal hydroxide array catalyst and its preparation method and application

Country Status (1)

Country Link
CN (1) CN106807349A (en)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107308958A (en) * 2017-06-12 2017-11-03 首都师范大学 A kind of oxygen evolution reaction electrochemical catalyst and its preparation and application
CN107630227A (en) * 2017-08-04 2018-01-26 天津理工大学 A kind of method that three-D nano-porous copper mesh elctro-catalyst is prepared based on metal net
CN109628952A (en) * 2018-12-31 2019-04-16 武汉工程大学 A kind of Ni-based double-metal hydroxide electrocatalytic hydrogen evolution catalyst of foamed nickel supported Ag doping and preparation method thereof
CN110965076A (en) * 2019-12-06 2020-04-07 吉林大学 Preparation method of electrolytic water electrode with double-function three-dimensional layered core-shell structure
CN111962099A (en) * 2020-08-20 2020-11-20 中国科学院宁波材料技术与工程研究所 Electrode for electrocatalytic production of hydrogen peroxide, preparation method and application thereof
WO2021143151A1 (en) * 2020-01-16 2021-07-22 厦门大学 Catalyst, preparation method therefor, and process for electrocatalytic decomposition of water into hydrogen
WO2021143152A1 (en) * 2020-01-16 2021-07-22 厦门大学 Catalyst, preparation method, and use in hydrogen production by water electrolysis
CN113774398A (en) * 2020-06-08 2021-12-10 清华大学 Method for producing hydrogen by selective oxidation coupling of alcohol or aldehyde
CN113943950A (en) * 2021-11-18 2022-01-18 西安工业大学 Multi-metal hydroxide pre-catalyst and preparation method and application thereof
CN115679370A (en) * 2022-11-16 2023-02-03 吉林大学 Transition metal catalyst and preparation method thereof

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105810957A (en) * 2016-03-25 2016-07-27 青岛大学 Preparation and application of platinum/nickel hydroxide-cobalt hydroxide/graphene three-dimensional composite catalyst

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105810957A (en) * 2016-03-25 2016-07-27 青岛大学 Preparation and application of platinum/nickel hydroxide-cobalt hydroxide/graphene three-dimensional composite catalyst

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
冯玉杰,等: "《环境工程中的功能材料》", 3 August 2003, 化学工业出版社 *

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107308958A (en) * 2017-06-12 2017-11-03 首都师范大学 A kind of oxygen evolution reaction electrochemical catalyst and its preparation and application
CN107308958B (en) * 2017-06-12 2019-11-05 首都师范大学 A kind of oxygen evolution reaction electrochemical catalyst and its preparation and application
CN107630227A (en) * 2017-08-04 2018-01-26 天津理工大学 A kind of method that three-D nano-porous copper mesh elctro-catalyst is prepared based on metal net
CN109628952A (en) * 2018-12-31 2019-04-16 武汉工程大学 A kind of Ni-based double-metal hydroxide electrocatalytic hydrogen evolution catalyst of foamed nickel supported Ag doping and preparation method thereof
CN110965076A (en) * 2019-12-06 2020-04-07 吉林大学 Preparation method of electrolytic water electrode with double-function three-dimensional layered core-shell structure
WO2021143151A1 (en) * 2020-01-16 2021-07-22 厦门大学 Catalyst, preparation method therefor, and process for electrocatalytic decomposition of water into hydrogen
WO2021143152A1 (en) * 2020-01-16 2021-07-22 厦门大学 Catalyst, preparation method, and use in hydrogen production by water electrolysis
CN113774398A (en) * 2020-06-08 2021-12-10 清华大学 Method for producing hydrogen by selective oxidation coupling of alcohol or aldehyde
CN111962099A (en) * 2020-08-20 2020-11-20 中国科学院宁波材料技术与工程研究所 Electrode for electrocatalytic production of hydrogen peroxide, preparation method and application thereof
CN111962099B (en) * 2020-08-20 2022-06-17 中国科学院宁波材料技术与工程研究所 Electrode for electrocatalytic production of hydrogen peroxide, preparation method and application thereof
CN113943950A (en) * 2021-11-18 2022-01-18 西安工业大学 Multi-metal hydroxide pre-catalyst and preparation method and application thereof
CN115679370A (en) * 2022-11-16 2023-02-03 吉林大学 Transition metal catalyst and preparation method thereof

Similar Documents

Publication Publication Date Title
CN106807349A (en) A kind of nano metal simple substance modification transition metal hydroxide array catalyst and its preparation method and application
CN105251513B (en) The electro-deposition preparation method of carbon nanotube/transistion metal compound composite material
CN105780049B (en) A kind of Trace Amounts of Platinum modification efficient liberation of hydrogen catalyst of molybdenum sulfide and preparation method thereof
CN107904614B (en) A kind of Ni3S2@Ni-Fe LDH analyses oxygen electro catalytic electrode and the preparation method and application thereof
CN105013512A (en) Self-supporting transitional metal sulfide catalyst and preparation methods and applications thereof
CN104923268A (en) Self-support transition metal selenide catalyst as well as preparation method and application thereof
CN107723735B (en) A kind of nano metal nickel and nickel oxide modification tungsten disulfide array catalyst and its preparation method and application
CN109659143A (en) A kind of nickel hydroxide/three nickel of curing/foam nickel composite and the preparation method and application thereof
CN104862758B (en) A kind of aquatic products hydrogen that decomposes is with NiS/Ni (OH)2The preparation method of elctro-catalyst
Xue et al. Ruthenium-nickel-cobalt alloy nanoparticles embedded in hollow carbon microtubes as a bifunctional mosaic catalyst for overall water splitting
CN110055557A (en) A kind of three-dimensional nickel doped iron base oxygen-separating catalyst and its preparation method and application
CN105107535A (en) Self-supporting transition metal-phosphorus alloy catalyst, and preparation method and application thereof
CN109954503A (en) A kind of nickelous selenide and ternary selenizing ferronickel composite electrocatalyst and preparation method and application
CN105780050B (en) A kind of preparation method for decomposing the doping phosphoric acid group Ni-Fe hydroxide nano film catalysts of water
CN105148920A (en) Self-supporting transition metal-metal alloy catalyst as well as preparation method and application of self-supporting transition metal-metal alloy catalyst
CN108671944A (en) A kind of nickel molybdenum oxide@nickel molybdenum sulphide@nickel foam composite nano materials and the preparation method and application thereof
CN106757143A (en) A kind of water decomposition reaction catalysis electrode and preparation method thereof
CN110021758A (en) The Pt-M metal alloy catalyst that in organic system prepared by electro-deposition
CN105177621B (en) Molybdenum-oxygen cluster modified hollow microspherical nickel disulfide catalyst and application thereof
CN110433829A (en) A kind of MoO2-NiSxThe agent of/CC Electrocatalytic Activity for Hydrogen Evolution Reaction and preparation method
CN107326395B (en) A kind of preparation method of the compound hydrogen-precipitating electrode of carbosphere of nickel/N doping
CN108722453A (en) A kind of phosphating sludge/carbon composite nano-material for alkaline electrocatalytic hydrogen evolution
CN105731463A (en) Preparation method and application of molybdenum carbide microspheres
CN109126825A (en) A kind of nickel doping Co9S8Nanometer sheet bifunctional electrocatalyst and preparation method thereof
CN112808274A (en) High-performance iron-doped nickel or cobalt-based amorphous oxyhydroxide catalyst prepared by room temperature method and research on efficient water electrolysis hydrogen production 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
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20170609

WD01 Invention patent application deemed withdrawn after publication