CN113512736B - Method for preparing membrane electrode by electrochemical deposition and application thereof - Google Patents

Method for preparing membrane electrode by electrochemical deposition and application thereof Download PDF

Info

Publication number
CN113512736B
CN113512736B CN202110464506.8A CN202110464506A CN113512736B CN 113512736 B CN113512736 B CN 113512736B CN 202110464506 A CN202110464506 A CN 202110464506A CN 113512736 B CN113512736 B CN 113512736B
Authority
CN
China
Prior art keywords
membrane
solution
nafion
deionized water
membrane electrode
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.)
Active
Application number
CN202110464506.8A
Other languages
Chinese (zh)
Other versions
CN113512736A (en
Inventor
王丽华
仇智
汪前东
何敏
杨海军
宋延林
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.)
Institute of Chemistry CAS
Original Assignee
Institute of Chemistry 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 Institute of Chemistry CAS filed Critical Institute of Chemistry CAS
Priority to CN202110464506.8A priority Critical patent/CN113512736B/en
Publication of CN113512736A publication Critical patent/CN113512736A/en
Application granted granted Critical
Publication of CN113512736B publication Critical patent/CN113512736B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • 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
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00Electroplating: Baths therefor
    • C25D3/66Electroplating: Baths therefor from melts
    • C25D3/665Electroplating: Baths therefor from melts from ionic liquids
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/88Processes of manufacture
    • H01M4/8825Methods for deposition of the catalytic active composition
    • H01M4/8853Electrodeposition
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/88Processes of manufacture
    • H01M4/8878Treatment steps after deposition of the catalytic active composition or after shaping of the electrode being free-standing body
    • H01M4/8882Heat treatment, e.g. drying, baking
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/10Fuel cells with solid electrolytes
    • H01M8/1004Fuel cells with solid electrolytes characterised by membrane-electrode assemblies [MEA]
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • Y02P20/133Renewable energy sources, e.g. sunlight

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Manufacturing & Machinery (AREA)
  • General Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Metallurgy (AREA)
  • Inorganic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Fuel Cell (AREA)
  • Inert Electrodes (AREA)
  • Electrodes For Compound Or Non-Metal Manufacture (AREA)

Abstract

The invention discloses a method for preparing a membrane electrode by electrochemical deposition, and relates to the field of membrane electrode preparation methods. Firstly, a commercial Nafion membrane or a proton exchange membrane is subjected to specific pretreatment, then a layer of graphene is coated on the membrane, and platinum micro-nano particles are loaded through electrochemical deposition, so that the high dispersion of the platinum micro-nano particles on the graphene is realized, and the effects of keeping the activity of a catalyst and reducing the dosage are achieved. The special substance-ionic liquid can be added into the solution for electrochemical deposition, and because of its strong adsorption capacity, it can change the electrochemical characteristics of electrode and solution interface, raise electrodeposition current efficiency and improve electric crystallization condition. The invention has simple process and easy operation, obviously improves the interface between the proton exchange membrane and the catalyst, has high electrodeposition efficiency, can effectively improve the performance of the membrane electrode, and overcomes the defects of complicated equipment, large amount of used catalyst, easy dehydration and deformation of the membrane in the hot pressing process and the like of the existing hot pressing method.

Description

Method for preparing membrane electrode by electrochemical deposition and application thereof
Technical Field
The invention relates to the field of membrane electrode preparation, in particular to a method for preparing a membrane electrode by electrochemical deposition and application thereof.
Background
In recent years, the demand for energy has been increasing, and the demand for moving from fossil fuels to renewable energy sources, such as wind energy, solar energy, biomass energy, hydroelectric power generation, and geothermal energy, has been pressing. On the way to the low-carbon energy society, hydrogen plays an important role as a secondary energy carrier. In future sustainable energy systems, it is possible that electrolysis of water will become the mainstream way for electricity-gas coupled electricity supply, transportation, heating and chemical sectors.
Membrane Electrode Assembly (MEA) is a key component for the electrolysis of water and the reaction, energy conversion and mass transport in fuel cells, and includes Gas Diffusion Layer (GDL), Catalyst Layer (CL) and PEM (proton exchange membrane). The existing method for preparing the membrane electrode can be summarized into two modes, wherein the first mode is the preparation of a carrier-free catalyst layer, namely, a catalyst is deposited on the surface of a proton exchange membrane in a chemical or physical deposition mode; the second is the preparation of the carrier catalyst layer, namely, the carrier catalyst is synthesized firstly and then is coated on the proton exchange membrane. The first membrane electrode preparation mode is more favored at present, and specific methods thereof include a hot pressing method, a chemical immersion reduction method, a transfer method, an electrochemical deposition method and the like, wherein the hot pressing method is the most widely used membrane electrode preparation method at present and is the earliest preparation method. The hot pressing method is that the cathode and anode catalyst layers are attached to two sides of the proton exchange membrane and then placed on the supporting surface of a hot press for hot pressing, or catalyst particles and a certain amount of carrier PTFE are mixed to prepare a catalyst film layer, and then the catalyst film layer and the proton exchange membrane are hot pressed to obtain the membrane electrode. The method has complicated equipment and large amount of used catalyst, and the membrane is easy to dehydrate and deform in the hot pressing process to influence the performance of the membrane.
The electrochemical deposition method is a membrane electrode preparation method with simple process and easy operation. In the previous researches, platinum is deposited on a diffusion layer carbon paper containing conductive carbon black or a carbon black carrier bonded by polytetrafluoroethylene, and then the carbon black carrier is directly assembled or hot-pressed with a proton exchange membrane.
Disclosure of Invention
The invention aims to overcome the defects of the prior art and provides a preparation method which is simple in process, easy to operate, high in electrodeposition efficiency and capable of obviously improving the interface between a proton exchange membrane and a catalyst and effectively improving the performance of a membrane electrode.
In order to achieve the above object, the present invention provides a method for preparing a membrane electrode by electrochemical deposition, comprising the following steps:
(1) pretreating a commercial Nafion membrane or a proton exchange membrane to prepare a base membrane of the membrane electrode;
(2) dissolving graphene slurry in a solvent, performing ultrasonic dispersion for 30-60 min, and coating the solution on the base membrane obtained in the step 1) to obtain a base membrane containing graphene;
(3) dissolving a platinum precursor, hydrochloric acid and ionic liquid in deionized water to prepare electrodeposition liquid or dissolving the platinum precursor, sodium dihydrogen phosphate, ammonium dihydrogen phosphate and the ionic liquid in deionized water to prepare electrodeposition liquid;
(4) in an electrochemical deposition device, taking the bottom film containing graphene prepared in the step 2) as a cathode, taking a titanium-coated platinum screen plate as an anode, electrifying and depositing for 30-90 min at a certain temperature and constant current density, cleaning the surface of the bottom film containing graphene after the electrifying and depositing by using deionized water, and drying to prepare a membrane electrode;
(5) preparing a solution from a Nafion solution and isopropanol according to a certain proportion, coating the solution on the surface of the membrane electrode obtained in the step 4), cleaning with deionized water and drying to obtain the membrane electrode.
According to the invention, the step 1) commercial Nafion membrane is Nafion115 or Nafion 117.
According to the invention, the proton exchange membrane in the step 1) is one of polybenzimidazole, sulfonated polysulfone, sulfonated polyetherimide, sulfonated polyether ether ketone or sulfonated polyaryletherketone.
According to the invention, the pretreatment mode of the Nafion membrane in the step 1) is as follows: sequentially passing a Nafion membrane through H with the mass concentration of 2-5% 2 O 2 The water solution is subjected to heat treatment at 60-80 ℃ for 30-60 min, washed by deionized water, 0.5-1 mol/L sulfuric acid solution is subjected to heat treatment at 60-80 ℃ for 30-60 min, and washed by deionized water and subjected to heat treatment at 60-80 ℃ for 30-60 min by deionized water.
According to the invention, the pretreatment mode of the proton exchange membrane in the step 1) is as follows: and soaking the membrane in 1-3 mol/L acid water solution for 2-7 days.
According to the invention, the acid is one of sulphuric acid, hydrochloric acid, formic acid, methanesulphonic acid or phosphoric acid.
According to the invention, the graphene slurry in the step 2) is aqueous conductive graphene slurry.
According to the invention, the concentration of the graphene slurry in the step 2) is 0.08-0.16 g/mL.
According to the invention, the solvent in the step 2) is an ethanol water solution or an isopropanol water solution, and the concentration of the ethanol water solution or the isopropanol water solution is 2.5-5 mg/mL;
preferably, a Nafion solution with the mass concentration of 5-10% can be added into the solution, wherein the mass ratio of the Nafion solution to the graphene slurry is 0.15-0.5.
According to the invention, the coating mode in the step 2) is air gun spraying or spin coating by a spin coater.
According to the invention, the platinum precursor in the step 3) is chloroplatinic acid or tetraammineplatinum dichloride, and the ionic liquid is imidazolyl ionic liquid;
preferably, the ionic liquid is one or a mixture of more of 1-ethyl-3-methyl-imidazole tetrafluoroborate, brominated 1-ethyl-3-methyl imidazole salt, 1-ethyl-3-methyl imidazole hexafluorophosphate or 1-butyl-3-methyl imidazole chloride salt.
According to the invention, the mass ratio of the hydrochloric acid to the platinum precursor in the electrodeposition liquid in the step 3) is 5-40.
According to the invention, the mass ratio of the sodium dihydrogen phosphate and the ammonium dihydrogen phosphate to the platinum precursor in the electrodeposition liquid in the step 3) is 5-40.
According to the invention, the content of the ionic liquid in the electrodeposition liquid in the step 3) is 10-50 mg/L, and preferably 30-50 mg/L.
According to the invention, the temperature in the step 4) is 30-70 ℃, and the current is 0.5-2.5A/dm 2
According to the invention, the mass concentration of the Nafion solution in the step 5) is 15-20%, and the volume ratio of the Nafion solution to the isopropanol is 0.5-2.
According to the invention, the coating mode in the step 5) is air gun spraying or spin coating by a spin coater.
It is another object of the present invention to provide a membrane electrode for use in an electrolytic water or hydrogen fuel cell.
The technical scheme of the invention has the following beneficial effects:
(1) the method is different from the traditional membrane electrode preparation (firstly preparing the Pt/C catalyst and then fixing the Pt/C catalyst on the proton exchange membrane), adopts a layer-by-layer assembly mode, namely firstly fixing the graphene slurry on the proton exchange membrane, and then depositing a layer of platinum micro-nano particles on the surface layer of the graphene by adopting an electrochemical deposition method, can effectively reduce the interface internal resistance between the catalyst and the proton exchange membrane, and provides a new idea for the preparation of the membrane electrode.
(2) According to the invention, the graphene and the platinum micro-nano particles are sequentially deposited on the surface layer of the proton exchange membrane, so that the platinum micro-nano particles are highly dispersed on the graphene, and the effects of keeping the activity of the catalyst and reducing the dosage are achieved.
(3) The invention takes a trace amount of ionic liquid as an additive of the metal electrodeposition solution, and the ionic liquid has physicochemical properties of higher chemical and thermal stability, higher ionic conductivity, stronger adsorption capacity and the like. Because of its strong adsorption capacity, it can change the electrochemical characteristics of electrode and solution interface, raise electrodeposition current efficiency and improve electric crystallization condition.
Drawings
FIG. 1 is a schematic structural diagram corresponding to each step of the membrane electrode preparation method of the present invention;
fig. 2 is a surface electron micrograph of the membrane electrode prepared in example 1 of the present invention.
Detailed Description
Embodiments of the present invention will be described in more detail below.
Example 1
(1) A5 cm × 5cm Nafion115 membrane was placed in 5% H 2 O 2 Heat treating in water solution at 80 deg.C for 30min, repeatedly washing the membrane with deionized water, soaking the membrane in 80 deg.C deionized water, and heat treating for 30 min; then carrying out heat treatment for 30min at 80 ℃ in 0.5mol/L dilute sulfuric acid aqueous solution; repeatedly washing the membrane with deionized water, soaking the membrane in 80 deg.C deionized water for heat treatment for 30min, and naturally cooling;
(2) weighing 0.125g of ethanol, dissolving in 50mL of deionized water, and preparing a dilute ethanol aqueous solution; weighing 5g of graphene slurry (solid content is 3-18%, particle size is 7-12 microns, the number of graphene layers is less than 10), dissolving 1g of Nafion solution with mass concentration of 5% in the dilute ethanol aqueous solution, performing ultrasonic dispersion for 40min, and spraying the mixed solution onto the Nafion115 membrane prepared in the step (1) by using an air gun to prepare a base membrane containing graphene;
(3) weighing 1g of chloroplatinic acid, 6g of hydrochloric acid and 20mg of ionic liquid (1-ethyl-3-methylimidazolium hexafluorophosphate) and dissolving in 400mL of deionized water to prepare an electrodeposition solution; and (3) taking a titanium platinum-coated screen plate as an anode, taking the graphene-containing basement membrane prepared in the equal-area step (2) as a cathode, placing the cathode in an electrochemical deposition device, controlling the temperature of a constant-temperature water bath at 65 ℃, stirring, supplying power by a direct-current stabilized power supply, controlling the constant current, and controlling the stable current to be 1.5A/dm 2 Electrifying for electrodeposition for 60min, and after the electrodeposition is finished, cleaning the surface of the membrane by deionized water and drying to obtain a membrane electrode;
(4) mixing a 15% Nafion solution and isopropanol in a volume ratio of 1: 2 preparing a solution, spraying the solution on the surface of the membrane electrode prepared in the step (3), washing the surface of the membrane with deionized water, and drying to obtain the membrane electrode.
Example 2
(1) A5 cm × 5cm Nafion117 membrane was placed in 5% H 2 O 2 Heat treating in water solution at 80 deg.C for 30min, repeatedly washing the membrane with deionized water, soaking the membrane in 80 deg.C deionized water, and heat treating for 30 min; then carrying out heat treatment for 30min at 80 ℃ in 0.5mol/L dilute sulfuric acid aqueous solution; repeatedly washing the membrane with deionized water, soaking the membrane in 80 deg.C deionized water, heat treating for 30min, and naturally cooling.
(2) Weighing 0.125g of ethanol, dissolving the ethanol in 50mL of deionized water to prepare a dilute ethanol aqueous solution, weighing 8g of graphene slurry (with solid content of 3-18%, particle size of 7-12 microns and graphene layer number of less than 10 layers) and 4g of Nafion solution with mass concentration of 5%, dissolving the graphene slurry in the dilute ethanol aqueous solution, performing ultrasonic dispersion for 60min, and spin-coating the mixed solution on the Nafion117 film prepared in the step (1) by using a spin coater to prepare the base film containing graphene.
(3) Weighing 0.8g of tetraammineplatinum dichloride, 24g of sodium dihydrogen phosphate, 12g of ammonium dihydrogen phosphate and 12mg of ionic liquid (1-ethyl-3-methyl-imidazole tetrafluoroborate) and dissolving in 400mL of deionized water to prepare an electrodeposition solution; then, a titanium platinum-coated screen plate is used as an anode, the bottom membrane containing graphene prepared in the equal-area step (2) is used as a cathode, the cathode is placed in an electrochemical deposition device, the temperature of the bottom membrane is controlled by a constant-temperature water bath kettle at 30 ℃, and the process is carried out until the temperature is controlledThe current stabilized power supply supplies power, the constant current is controlled, and the stable current is 1.0A/dm 2 Electrifying for electrodeposition for 90min, and after the electrodeposition is finished, cleaning the surface of the membrane by deionized water and drying to obtain a membrane electrode;
(4) mixing a 20% Nafion solution and isopropanol in a volume ratio of 1: 2 preparing a solution, spraying the solution on the surface of the membrane electrode prepared in the step (3), washing the surface of the membrane with deionized water, and drying to obtain the membrane electrode.
Example 3
(1) Soaking a polybenzimidazole membrane with the size of 5cm multiplied by 5cm in a sulfuric acid aqueous solution of 3mol/L for 7 days, repeatedly washing the polybenzimidazole membrane by deionized water, and naturally cooling the membrane.
(2) Weighing 0.25g of ethanol, dissolving the ethanol in 50mL of deionized water to prepare a dilute ethanol aqueous solution, weighing 4g of graphene slurry (solid content is 3-18%, particle size is 7-12 microns, the number of graphene layers is less than 10 layers), dissolving the graphene slurry in the dilute ethanol aqueous solution, performing ultrasonic dispersion for 60min, and spraying the mixed solution onto the proton exchange membrane prepared in the step (1) by using an air gun to prepare a base membrane containing graphene;
(3) dissolving 1g of chloroplatinic acid, 5g of hydrochloric acid and 16mg of ionic liquid (1-ethyl-3-methyl-imidazole tetrafluoroborate) in 400mL of deionized water to prepare an electrodeposition solution; and (3) placing the titanium-coated platinum screen plate serving as an anode and the graphene-containing bottom membrane prepared in the equal-area step (2) serving as a cathode in an electrochemical deposition device, controlling the temperature in a constant-temperature water bath kettle at 70 ℃, stirring, supplying power by a direct-current stabilized power supply, and controlling the constant current with the stable current of 2.5A/dm 2 Electrifying for electrodeposition for 30min, and after the electrodeposition is finished, cleaning the surface of the membrane by deionized water and drying to obtain a membrane electrode;
(4) mixing a 20% Nafion solution and isopropanol in a volume ratio of 1: 1 preparing a solution, spraying the solution on the surface of the membrane electrode prepared in the step (3), washing the surface of the membrane with deionized water, and drying to obtain the membrane electrode.
Example 4
(1) Soaking sulfonated polyether ether ketone with the size of 5cm multiplied by 5cm in 1mol/L hydrochloric acid water solution for 2 days, repeatedly washing with deionized water, and naturally cooling the membrane.
(2) Weighing 0.2g of isopropanol, dissolving the isopropanol in 50mL of deionized water to prepare an isopropanol aqueous solution, weighing 4g of graphene slurry (solid content is 3-18%, particle size is 7-12 mu m, number of graphene layers is less than 10 layers), dissolving 2g of Nafion solution with mass concentration of 5% in the diluted isopropanol aqueous solution, performing ultrasonic dispersion for 30min, and spraying the mixed solution onto the proton exchange membrane prepared in the step (1) by using an air gun to prepare a base membrane containing graphene;
(3) dissolving 1g of chloroplatinic acid, 5g of hydrochloric acid and 20mg of ionic liquid (1-ethyl-3-methyl-imidazole tetrafluoroborate) in 400mL of deionized water to prepare an electrodeposition solution; and (3) placing the titanium-coated platinum screen plate serving as an anode and the graphene-containing bottom membrane prepared in the equal-area step (2) serving as a cathode in an electrochemical deposition device, controlling the temperature in a constant-temperature water bath kettle at 50 ℃, stirring, supplying power by a direct-current stabilized power supply, and controlling the constant current with the stable current of 0.5A/dm 2 Electrifying for electrodeposition for 60min, and after the electrodeposition is finished, cleaning the surface of the membrane by deionized water and drying to obtain a membrane electrode;
(4) mixing a 20% Nafion solution and isopropanol in a volume ratio of 1: 1 preparing a solution, spraying the solution on the surface of the membrane electrode prepared in the step (3), washing the surface of the membrane with deionized water, and drying to obtain the membrane electrode.

Claims (13)

1. A method for preparing a membrane electrode by electrochemical deposition is characterized by comprising the following steps:
1) pretreating a commercial Nafion membrane or a proton exchange membrane to prepare a base membrane of the membrane electrode;
2) dissolving graphene slurry in a solvent, performing ultrasonic dispersion for 30-60 min, and coating the solution on the base membrane obtained in the step 1) to obtain a base membrane containing graphene;
3) dissolving a platinum precursor, hydrochloric acid and ionic liquid in deionized water to prepare an electrodeposition liquid, or dissolving the platinum precursor, sodium dihydrogen phosphate, ammonium dihydrogen phosphate and ionic liquid in deionized water to prepare the electrodeposition liquid;
4) in an electrochemical deposition device, taking the bottom film containing graphene prepared in the step 2) as a cathode, taking a titanium-coated platinum screen plate as an anode, performing energization deposition for 30-90 min at a certain temperature and constant current density, cleaning the surface of the bottom film containing graphene after the energization deposition by using deionized water, and drying to prepare a membrane electrode;
5) preparing a solution from a Nafion solution and isopropanol according to a certain proportion, coating the solution on the surface of the membrane electrode obtained in the step 4), cleaning with deionized water, and drying to obtain the membrane electrode.
2. The method as claimed in claim 1, wherein the commercial Nafion membrane in step 1) is Nafion115 or Nafion 117; the proton exchange membrane is one of polybenzimidazole, sulfonated polysulfone, sulfonated polyetherimide, sulfonated polyether-ether-ketone or sulfonated polyaryletherketone.
3. The method as claimed in claim 1, wherein the Nafion membrane pretreatment mode in the step 1) is as follows: sequentially passing a Nafion membrane through H with the mass concentration of 2-5% 2 O 2 Heat-treating the aqueous solution at 60-80 ℃ for 30-60 min, washing with deionized water, heat-treating 0.5-1 mol/L sulfuric acid solution at 60-80 ℃ for 30-60 min, washing with deionized water and heat-treating the deionized water at 60-80 ℃ for 30-60 min; the pretreatment mode of the proton exchange membrane is as follows: and soaking the membrane in 1-3 mol/L acid water solution for 2-7 days.
4. The method of claim 3, wherein the acid is one of sulfuric acid, hydrochloric acid, formic acid, methanesulfonic acid, or phosphoric acid.
5. The method according to claim 1, wherein the graphene slurry in the step 2) is an aqueous conductive graphene slurry; the concentration of the graphene slurry is 0.08-0.16 g/mL; the solvent is an ethanol water solution or an isopropanol water solution, and the concentration of the solvent is 2.5-5 mg/mL; the coating mode is air gun spraying or spin coating by a spin coater.
6. The method according to claim 1, wherein a Nafion solution with a mass concentration of 5-10% is added to the solution in the step 2), and the mass ratio of the Nafion solution to the graphene slurry is 0.15-0.5.
7. The method according to claim 1, wherein the platinum precursor in step 3) is chloroplatinic acid or tetraammineplatinum dichloride; the ionic liquid is imidazolyl ionic liquid.
8. The method according to claim 1, wherein the ionic liquid in the step 3) is one or a mixture of more of 1-ethyl-3-methyl-imidazole tetrafluoroborate, brominated 1-ethyl-3-methyl imidazole salt, 1-ethyl-3-methyl imidazole hexafluorophosphate or 1-butyl-3-methyl imidazole chloride salt.
9. The method according to claim 1, wherein the mass ratio of the hydrochloric acid to the platinum precursor in the electrodeposition solution of step 3) is 5 to 40; the mass ratio of the sodium dihydrogen phosphate to the ammonium dihydrogen phosphate to the platinum precursor in the electrodeposition liquid is 5-40; the content of the ionic liquid in the electrodeposition liquid is 10-50 mg/L.
10. The method of claim 1, wherein the ionic liquid content of the electrodeposition solution in the step 3) is 30-50 mg/L.
11. The method as claimed in claim 1, wherein the temperature in step 4) is 30 to 70 ℃ and the current is 0.5 to 2.5A/dm 2
12. The method according to claim 1, wherein the mass concentration of the Nafion solution in the step 5) is 15-20%, and the volume ratio of the Nafion solution to the isopropanol is 0.5-2; the coating mode is air gun spraying or spin coating by a spin coater.
13. Use of a membrane electrode prepared according to any one of claims 1 to 12 in an electrolytic water or hydrogen fuel cell.
CN202110464506.8A 2021-04-28 2021-04-28 Method for preparing membrane electrode by electrochemical deposition and application thereof Active CN113512736B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202110464506.8A CN113512736B (en) 2021-04-28 2021-04-28 Method for preparing membrane electrode by electrochemical deposition and application thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202110464506.8A CN113512736B (en) 2021-04-28 2021-04-28 Method for preparing membrane electrode by electrochemical deposition and application thereof

Publications (2)

Publication Number Publication Date
CN113512736A CN113512736A (en) 2021-10-19
CN113512736B true CN113512736B (en) 2022-08-26

Family

ID=78063754

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202110464506.8A Active CN113512736B (en) 2021-04-28 2021-04-28 Method for preparing membrane electrode by electrochemical deposition and application thereof

Country Status (1)

Country Link
CN (1) CN113512736B (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114318403B (en) * 2021-12-31 2023-08-25 上海大学 Method for preparing platinum monoatomic material by adopting alkyl imidazole ionic liquid
CN114807958B (en) * 2022-06-08 2024-05-07 中国科学院化学研究所 High specific surface area proton exchange membrane electrode and preparation method thereof

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106159283A (en) * 2015-04-08 2016-11-23 宜兴市四通家电配件有限公司 A kind of membrane electrode of fuel batter with proton exchange film and preparation method thereof
CN105905993A (en) * 2016-06-14 2016-08-31 北京工业大学 Method for preparing supported palladium catalyst electrode on basis of graphene-doped Nafion film modification
CN109560310B (en) * 2017-09-25 2022-04-29 粟青青 Fuel cell ultra-low platinum loading self-humidifying membrane electrode and preparation method thereof
CN109449466B (en) * 2018-10-23 2020-11-24 山东潍氢动力科技有限公司 Preparation method of membrane electrode and preparation method of anode catalyst layer of membrane electrode
CN111244487B (en) * 2019-02-14 2021-03-26 南京攀峰赛奥能源科技有限公司 Proton exchange membrane fuel cell electrode catalyst, preparation method and proton exchange membrane fuel cell

Also Published As

Publication number Publication date
CN113512736A (en) 2021-10-19

Similar Documents

Publication Publication Date Title
CN107858701B (en) A kind of titanium-based hydrogen-precipitating electrode and preparation method thereof for solid polymer water electrolyzer
CN113512736B (en) Method for preparing membrane electrode by electrochemical deposition and application thereof
CN109921041B (en) Preparation and application of non-noble metal nitrogen-doped hollow carbon nanotube electrocatalyst
CN102867967B (en) A kind of all-vanadium liquid flow energy storage battery electrode material and application thereof
CN103280583B (en) Method for preparing catalytic layer structure of proton exchange membrane fuel cell
CN104846397A (en) Electrode for electrochemical reduction of CO2 and preparation of formic acid and preparation method and application thereof
CN102881925A (en) Novel ordering membrane electrode and preparation method and application thereof
CN109037715A (en) A kind of ultralow platinum content catalyst and preparation method for fuel cell
CN107681163A (en) A kind of fuel cell membrane electrode and its preparation method and application
CN103123974A (en) Conducting polymer/metal/proton exchange composite membrane and preparation and application thereof
CN112481656B (en) Bifunctional catalyst for high-selectivity electrocatalysis of glycerin oxidation conversion to produce formic acid and high-efficiency electrolysis of water to produce hydrogen, preparation method and application thereof
CN106816614A (en) Preparation and electrode and application that fuel cell is catalyzed with fine and close platinum monoatomic layer
CN109273728A (en) A kind of pulse electrodeposition prepares Platinum Nanoparticles/cobalt titanium dioxide nanotube composite electrode method
CN103367768B (en) A kind of method preparing double-catalyst-layestructure structure of proton exchange membrane fuel cell
Ünlü et al. Improved gas diffusion electrodes for hybrid polymer electrolyte fuel cells
CN112980247A (en) High-stability ink-jet printing ink for fuel cell and preparation and application thereof
CN103779582A (en) Method for preparing fuel cell membrane electrode
CN1683596A (en) Method for producing hydrogen and storaging hydrogen integrately
CN109860633A (en) The preparation method and purposes of a kind of order mesoporous Catalytic Layer and membrane electrode
CN114079071B (en) Preparation method and application of self-supporting membrane electrode
CN114808000A (en) Construction method of efficient and stable PEM (proton exchange membrane) electrolyzed water anode catalyst layer
CN113314720B (en) Preparation method and application of patterned membrane electrode
Yuan et al. Converting CO2 to multi-carbon products at> 1 A/cm2 using gas diffusion electrode based on commercial materials via transfer process engineering
CN110783574A (en) Direct alcohol fuel cell gas diffusion electrode and preparation method thereof and direct alcohol fuel cell
CN104916851A (en) Production method of catalysis layer

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