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WO2019132281A1 - Catalyseur, son procédé de préparation, électrode le comprenant, ensemble membrane-électrode et pile à combustible - Google Patents

Catalyseur, son procédé de préparation, électrode le comprenant, ensemble membrane-électrode et pile à combustible Download PDF

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Publication number
WO2019132281A1
WO2019132281A1 PCT/KR2018/015195 KR2018015195W WO2019132281A1 WO 2019132281 A1 WO2019132281 A1 WO 2019132281A1 KR 2018015195 W KR2018015195 W KR 2018015195W WO 2019132281 A1 WO2019132281 A1 WO 2019132281A1
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Prior art keywords
phthalocyanine
catalyst
coating layer
carbon
group
Prior art date
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PCT/KR2018/015195
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English (en)
Korean (ko)
Inventor
김정호
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Kolon Industries Inc
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Kolon Industries Inc
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Priority claimed from KR1020180149343A external-priority patent/KR102323487B1/ko
Application filed by Kolon Industries Inc filed Critical Kolon Industries Inc
Priority to EP18893847.6A priority Critical patent/EP3734728A4/fr
Priority to US16/957,530 priority patent/US11831025B2/en
Priority to JP2020532966A priority patent/JP2021506573A/ja
Priority to CN201880083886.7A priority patent/CN111527633B/zh
Publication of WO2019132281A1 publication Critical patent/WO2019132281A1/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02—Impregnation, coating or precipitation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/04—Mixing
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/08—Heat treatment
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/34—Irradiation by, or application of, electric, magnetic or wave energy, e.g. ultrasonic waves ; Ionic sputtering; Flame or plasma spraying; Particle radiation
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/90—Selection of catalytic material
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/90—Selection of catalytic material
    • H01M4/92—Metals of platinum group
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/10—Fuel cells with solid electrolytes
    • H01M8/1004—Fuel cells with solid electrolytes characterised by membrane-electrode assemblies [MEA]
    • 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
    • Y02E60/50—Fuel cells
    • 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
    • Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50—Manufacturing or production processes characterised by the final manufactured product

Definitions

  • the present invention relates to a catalyst, a method for producing the same, an electrode, a membrane-electrode assembly and a fuel cell comprising the same, and more particularly to a method for forming a coating layer on a catalyst surface
  • the durability is improved and the catalyst including the coating layer is post-treated to form a carbon coating layer. Further, durability is further improved, and the carbon nanofibers or carbon nanotubes produced during the post-treatment process have improved mass transfer performance and performance Catalyst, a method for producing the same, an electrode including the same, a membrane-electrode assembly, and a fuel cell.
  • a fuel cell is a power generation system that directly converts the chemical reaction energy of hydrogen and oxygen contained in a hydrocarbon-based material such as methanol, ethanol, and natural gas into electrical energy.
  • a typical example of such a fuel cell is a polymer electrolyte fuel cell (PEMFC).
  • PEMFC polymer electrolyte fuel cell
  • the PEMFC is attracting attention as a next-generation energy source, and in particular, research for commercialization has been actively conducted due to advantages such as environment-friendly images in the automobile related field.
  • a membrane electrode assembly that substantially generates electricity includes an anode electrode (also referred to as a fuel electrode or an oxidizing electrode) sandwiching a polymer electrolyte membrane containing a proton conductive polymer, And a cathode electrode (aka, air electrode or reduction electrode) are located.
  • anode electrode also referred to as a fuel electrode or an oxidizing electrode
  • a cathode electrode aka, air electrode or reduction electrode
  • Each electrode is composed of a catalyst, an ionomer, a solvent and an additive, and the catalyst among the above components is a main factor determining the activity and durability of the fuel cell.
  • Pt / C catalysts having platinum nanoparticles supported on a carbon support having a large specific surface area and excellent electrical conductivity are the most widely used catalysts for the oxidizing and reducing electrodes.
  • the Pt / C catalyst is produced by using pure platinum, which is an expensive metal, and is a main cause of increasing the price of the catalyst.
  • the Pt / C catalyst is generated by oxygen adsorption on the platinum surface due to the oxygen reduction reaction of the reducing electrode, It is a major cause of the delay of commercialization by generating energy loss of about 30% due to overvoltage.
  • high-crystalline carbon such as graphitized carbon, carbon nanotubes, and graphene is utilized as a carrier to enhance durability.
  • high-crystalline carbon such as graphitized carbon, carbon nanotubes, and graphene is utilized as a carrier to enhance durability.
  • the catalyst particles are agglomerated or separated from the carrier by driving the fuel cell, which is fundamentally caused by the thermodynamic characteristic that the catalyst such as platinum dissolves through oxygen species, Development and corrosion of the carbon carrier.
  • Another object of the present invention is to provide a method for producing the catalyst.
  • Still another object of the present invention is to provide a fuel cell including the membrane-electrode assembly.
  • a method of manufacturing a semiconductor device comprising the steps of: forming a carrier, metal particles supported on the carrier, and metal particles on the surface of the carrier and containing phthalocyanine, M- phthalocyanine (where M is a transition metal) And a coating layer comprising any one selected from the group consisting of a mixture of two or more of the foregoing.
  • a carbon coating composition comprising a support, metal particles supported on the support, and a coating layer positioned on the surfaces of the metal particles and the support, wherein the coating layer is a carbon coating layer containing hetero- ≪ / RTI >
  • the carbon coating layer may be one in which any one selected from the group consisting of phthalocyanine, M-phthalocyanine (where M is a transition metal), and a mixture thereof is carbonized.
  • the hetero element may be any one selected from the group consisting of nitrogen, transition metal, and both.
  • the coating layer may further include any one selected from the group consisting of carbon nanofibers, carbon nanotubes, and mixtures thereof on the whole or part of the surface of the carbon coating layer.
  • the carbon coating layer may be one in which any one selected from the group consisting of phthalocyanine, M-phthalocyanine (where M is a transition metal), and a mixture thereof is carbonized.
  • Any one selected from the group consisting of carbon nanofibers, carbon nanotubes, and mixtures thereof may be grown from the carbon coating layer.
  • the length of the carbon nanofibers or carbon nanotubes may be 50 nm to 5,000 nm.
  • M which is a transition metal of M-phthalocyanine, may be any one selected from the group consisting of Fe, Co, Cu, Ti, Ni, Zn, Mn and combinations thereof.
  • the thickness of the coating layer may be 0.1 nm to 7 nm.
  • the content of the coating layer may be 5 wt% to 30 wt% with respect to the total weight of the catalyst.
  • the content of any one selected from the group consisting of carbon nanofibers, carbon nanotubes, and mixtures thereof may be 1 wt% to 10 wt% with respect to the total weight of the catalyst.
  • the catalyst may further include a carrier and a second catalyst including metal particles supported on the carrier.
  • a method of manufacturing a semiconductor device which comprises mixing metal particles carried on a carrier with any one selected from the group consisting of phthalocyanine, M-phthalocyanine (where M is a transition metal) And coating the surface of the metal particles and the support with any one selected from the group consisting of phthalocyanine, M-phthalocyanine, and mixtures thereof.
  • the mixing may be carried out by mixing any one selected from the group consisting of a metal particle supported on the carrier and a phthalocyanine, M-phthalocyanine, and a mixture thereof in a solid phase, such as a ball mill, a powder mixer and a resonance acoustic mixer May be mixed with each other.
  • the resonance acoustic mixer may be configured to apply low-frequency acoustic energy to any one selected from the group consisting of the metal particles supported on the support and the phthalocyanine, M-phthalocyanine, and a mixture thereof to form resonant vibratory mixing.
  • the low frequency acoustic energy may have a frequency of 10 to 100 Hz.
  • the resonance mixing may be performed for 30 seconds to 30 minutes by applying an acceleration of 10 to 100 G to any one selected from the group consisting of the metal particles supported on the carrier and the phthalocyanine, M-phthalocyanine and mixtures thereof.
  • the method may further include a step of heat-treating any one selected from the group consisting of phthalocyanine, M-phthalocyanine, and mixtures thereof to form a carbon coating layer containing carbon doped with the hetero element.
  • the carbon coating layer is formed by carbonizing at least one selected from the group consisting of carbon nanofibers, carbon nanotubes, and mixtures thereof in the whole or part of the carbon coating layer when the carbon nanotubes are carbonized through the heat treatment. One can grow.
  • the heat treatment may be performed at 400 ° C. to 800 ° C. for 5 minutes to 60 minutes.
  • the heat treatment may be performed in an argon or argon-hydrogen (H 2 -Ar) atmosphere.
  • an electrode comprising the catalyst and an ionomer.
  • a plasma display panel comprising an anode electrode and a cathode electrode facing each other, and an ion exchange membrane disposed between the anode electrode and the cathode electrode, wherein the anode electrode, Wherein at least one of the electrodes selected from the group consisting of the electrodes comprises the electrode.
  • a fuel cell including the membrane-electrode assembly.
  • the catalyst of the present invention is improved in durability by forming a coating layer on the surface of the catalyst through a comparatively easy method without any treatment of a conventional catalyst or a conventional catalyst and by post-treating the catalyst containing the coating layer to form a carbon coating layer, As a result, carbon nanofibers or carbon nanotubes produced during the post-treatment process have improved mass transfer performance and performance.
  • FIG. 1 is a schematic diagram schematically showing a catalyst according to an embodiment of the present invention.
  • FIG. 2 is a schematic diagram schematically showing a catalyst according to another embodiment of the present invention.
  • FIG. 3 is a schematic diagram schematically showing catalysts of different shapes according to another embodiment of the present invention.
  • FIG. 4 is a schematic view showing an overall process procedure of a catalyst manufacturing method according to an embodiment of the present invention.
  • FIG. 5 is a schematic cross-sectional view of a membrane-electrode assembly according to an embodiment of the present invention.
  • FIG. 6 is a schematic diagram showing the overall configuration of a fuel cell according to an embodiment of the present invention.
  • TEM 7 and 8 are transmission electron microscope (TEM) photographs of the coated catalyst before heat treatment prepared in Example 1 of the present invention.
  • Example 9 is a transmission electron microscope (TEM) photograph of the commercial catalyst used in Example 1 of the present invention.
  • Example 10 is a transmission electron microscope (TEM) photograph of the catalyst prepared in Example 3 of the present invention.
  • Example 11 is a scanning electron microscope (SEM) photograph of the catalyst prepared under the argon atmosphere prepared in Example 2 of the present invention.
  • Example 12 is a scanning electron microscope (SEM) photograph of the catalyst prepared in the argon-hydrogen mixed gas atmosphere produced in Example 3 of the present invention.
  • Example 13 is a graph showing changes in catalytic active area at the beginning of the CV (Cyclo-voltammetry) evaluation and after 10,000 cycles measured in Experimental Example 2 of the present invention.
  • the catalyst according to an embodiment of the present invention includes a support, metal particles supported on the support, and a coating layer positioned on the surfaces of the metal particles and the support.
  • the carrier may be selected from a carbon-based carrier, porous inorganic oxides such as zirconia, alumina, titania, silica, and ceria, zeolite, and the like.
  • the carbon carrier may be selected from the group consisting of super P, carbon fiber, carbon sheet, carbon black, Ketjen black, acetylene black, but are not limited to, carbon nanotube (CNT), carbon sphere, carbon ribbon, fullerene, activated carbon, and combinations of one or more thereof.
  • Carriers which can be used in the technical field can be used without limitation.
  • the metal particles carried on the carrier may be located on the surface of the carrier or may penetrate into the carrier while filling the pores of the carrier.
  • the metal particles may be any of those which can be used as a catalyst for a hydrogen oxidation reaction or an oxygen reduction reaction, and a platinum group metal may be preferably used.
  • the platinum group metal may be at least one selected from the group consisting of platinum (Pt), palladium (Pd), ruthenium (Ru), iridium (Ir), osmium (Os), platinum-M alloy (M is palladium (Pd), ruthenium (Ir), Os, Ga, Ti, V, Cr, Mn, Fe, Co, Ni, And at least one selected from the group consisting of Cu, Ag, Au, Zn, Sn, Mo, W, La, Or more), and combinations thereof. More preferably, a combination of two or more metals selected from the platinum-based catalyst metal group may be used, but the present invention is not limited thereto. Any platinum-based catalyst metal that can be used in the technical field of the invention can be used without limitation.
  • the metal particles may be contained in an amount of 20 wt% to 80 wt% based on the total weight of the catalyst. If the metal particles are contained in an amount of less than 20 wt%, the activity may deteriorate. When the metal particles are in an amount of more than 80 wt% The active area may be reduced and the catalytic activity may be reversely lowered.
  • the coating layer may be a first coating layer containing any one selected from the group consisting of phthalocyanine, M-phthalocyanine (where M is a transition metal), and mixtures thereof.
  • the coating layer may be a carbon coating layer containing carbon doped with a hetero element, or may be formed of a carbon nanofiber, a carbon nanotube, or a mixture thereof on the entire surface or a part of the surface of the carbon coating layer and / And a second coating layer including a second coating layer.
  • the coating layer covers and protects the metal particles and the surface of the carrier, thereby preventing the metal particles, such as platinum, from dissolving through oxygen species, thereby preventing the aggregation phenomenon and the desorption phenomenon of the metal particles, Corrosion can be prevented, and as a result, the durability of the catalyst can be improved.
  • the second coating layer may include any one selected from the group consisting of the carbon nanofibers, carbon nanotubes, and mixtures thereof formed on the entire surface or a part of the surface of the carbon coating layer according to the content of the phthalocyanine precursor.
  • the second coating layer containing the hetero-element-doped carbon covers and protects the surfaces of the metal particles to prevent the metal particles from aggregation and desorption, corrosion of the carrier, and enhance the durability of the catalyst.
  • the performance and durability of the catalyst can be improved by improving the mass transfer and the like by any one selected from the group consisting of the carbon nanofibers, the carbon nanotubes, and the mixture thereof present on the entire surface or part of the surface of the carbon coating layer .
  • the M may be any one selected from the group consisting of Fe, Co, Cu, Ti, Ni, Zn, Mn, and combinations thereof.
  • the first coating layer containing any one selected from the group consisting of phthalocyanine, M-phthalocyanine, and mixtures thereof may be carbonized through heat treatment to form a carbon coating layer containing carbon doped with the hetero element
  • a second coating layer including any one selected from the group consisting of carbon nanofibers, carbon nanotubes, and mixtures thereof present on all or part of the surface can be formed.
  • any one selected from the group consisting of carbon nanofibers, carbon nanotubes, and mixtures thereof may include carbon doped with the hetero-element.
  • the hetero-element-doped carbon may be one selected from the group consisting of phthalocyanine, M-phthalocyanine, and mixtures thereof.
  • the hetero-element may be a nitrogen atom contained in the phthalocyanine, or the M- phthalocyanine
  • the transition metal may be in a reduced form or an oxide form, and a part of the transition metal may be in the form of a metal alloy adjacent to the metal particle.
  • the second coating layer containing the hetero-element-doped carbon has a structure in which nitrogen atoms derived from the phthalocyanine are bonded to the carbon coating layer and the carbon nanofibers, carbon nanotubes, and mixtures thereof (Atomic%) to 3 atomic%.
  • the second coating layer containing the hetero-element-doped carbon may further include a transition metal derived from the M-phthalocyanine selected from the group consisting of the carbon coating layer and the carbon nanofibers, carbon nanotubes, and mixtures thereof (Atomic%) with respect to the entire one of them.
  • the carbon nanofibers, the carbon nanotubes, and the mixture thereof may be selected from the group consisting of the phthalocyanine, the M-phthalocyanine, and the mixture thereof. It can be grown in dimension. Any one selected from the group consisting of carbon nanofibers, carbon nanotubes, and mixtures thereof may further improve the mass transfer capability and performance of the catalyst.
  • the carbon nanofibers or carbon nanotubes may have a length of 50 nm to 5,000 nm, specifically 200 nm to 1,000 nm.
  • the length of the carbon nanofibers or carbon nanotubes is less than 50 nm, the effect of the invention can not be clearly shown due to insufficient mass transfer and performance improvement. If the length is more than 5,000 nm, have.
  • Any one selected from the group consisting of carbon nanofibers, carbon nanotubes, and mixtures thereof may be included in an amount of 1 wt% to 10 wt% based on the total weight of the catalyst, and specifically, 2 wt% to 7 wt% .
  • the content of any one selected from the group consisting of carbon nanofibers, carbon nanotubes, and mixtures thereof is less than 1 wt% based on the total weight of the catalyst, the effect of the present invention may be insignificant.
  • the content exceeds 10 wt% Performance may be degraded.
  • the thickness of the coating layer may be varied depending on the type of the metal particles and the type of the support, and the thickness of the coating layer may be controlled by adjusting the content of any one selected from the group consisting of phthalocyanine, M-phthalocyanine, and mixtures thereof .
  • the thickness of the coating layer is preferably as thin as possible, may be 0.1 nm to 7 nm, and may be specifically 1 nm to 3 nm. By making the thickness of the coating layer as thin as possible, the durability can be improved without lowering the activity of the catalyst.
  • the content of the coating layer may be 5 wt% to 30 wt%, and more preferably 7 wt% to 23 wt% with respect to the total weight of the catalyst. If the content of the coating layer is less than 5% by weight with respect to the total weight of the catalyst, there may occur a region where the metal particles are not coated. If the content of the coating layer is more than 30% by weight, the coating layer may have a large thickness, And the phenomenon that the phthalocyanine or the M-phthalocyanine coagulates may occur.
  • Figs. 1 to 3 are schematic views schematically showing respective embodiments of the coating layer. Fig.
  • the metal particles 2 are supported on the support 1, and the carbon coating layer 4 containing the hetero-element-doped carbon is deposited on the surface of the support 1, And covers the surface of the metal particles 2.
  • the catalyst may further include a second catalyst that does not include the coating layer in addition to the first catalyst including the coating layer. That is, the second catalyst may include the carrier and the metal particles supported on the carrier, and the description thereof is the same as that described above, so repetitive description will be omitted.
  • a method of manufacturing a catalyst according to another embodiment of the present invention is a method of preparing a catalyst, comprising the steps of: preparing a mixture of metal particles supported on a support and at least one selected from the group consisting of phthalocyanine, M-phthalocyanine (where M is a transition metal) And coating the surface of the metal particles and the carrier with one selected from the group consisting of phthalocyanine, M-phthalocyanine and mixtures thereof.
  • the metal particles supported on the support may be commercially available products or may be prepared by supporting the metal particles on the support. Since the process of supporting the metal particles on the carrier is widely known in the art, a detailed description thereof will not be given in this specification, so that it will be understood by those skilled in the art.
  • the mixing may be performed by mixing the metal particles carried on the carrier and any one selected from the group consisting of phthalocyanine, M-phthalocyanine and mixtures thereof in a solid phase.
  • the techniques for coating the catalyst include mixing the catalyst and a material for forming a coating layer in an aqueous solution.
  • the process involves a series of processes of dispersing and drying in an aqueous solution, And loss may occur.
  • the durability of the catalysts prepared by the above method can be improved by including the coating layer, the process is complicated and the yield may be significantly reduced.
  • the method of forming a coating layer of the present invention can be carried out in a solid phase so as to prevent damage and loss of the catalyst in the coating layer formation process, and to select a smaller amount of the phthalocyanine, M- phthalocyanine, Can be uniformly coated on the surface of the metal particles.
  • the coating layer is selected from the group consisting of metal particles supported on the solid support, a phthalocyanine, M-phthalocyanine, and a mixture thereof, and a ball mill, a powder mixer, and a resonance acoustic mixer They may be mixed using any one of them, and preferably, mixed using a resonance acoustic mixer.
  • the catalyst may be deformed.
  • the coating effect may not be sufficiently realized.
  • the resonance acoustic mixer by using the resonance acoustic mixer, a more uniform coating result can be obtained in a short time.
  • the resonance acoustic mixer applies low-frequency acoustic energy to metal particles supported on the support, and any one selected from the group consisting of phthalocyanine, M-phthalocyanine, and a mixture thereof, (resonant vibratory mixing).
  • the resonance mixing may be performed by applying a low frequency acoustic energy and the low frequency acoustic energy is a linear or spherical energy wave through a type medium in a frequency range of 10 to 20,000 Hz.
  • the carrier and the metal In order to coat the surface of the particle with any one selected from the group consisting of phthalocyanine, M-phthalocyanine and a mixture thereof, a low frequency acoustic energy having a frequency of 10 to 100 Hz, specifically 50 to 70 Hz, Can be used.
  • the resonance mixing may be carried out by mixing the metal particles supported on the carrier under the frequency with any one selected from the group consisting of phthalocyanine, M-phthalocyanine and mixtures thereof in an amount of 10 to 100 G, (Where, G means gravitational acceleration, for example, 10 G means 10 times the gravitational acceleration).
  • the acceleration When the acceleration is less than 10 G, an unmixed region may exist, and coating may not be performed to deteriorate the performance.
  • the acceleration exceeds 100 G, the phthalocyanine or the M-phthalocyanine may be aggregated or mixed by phase separation and heat generation There may be problems such as a change in condition and a decrease in performance.
  • the method for applying the low-frequency acoustic energy and the acceleration to the mixture in the frequency region is not particularly limited in the present invention, and any method known in the art can be used. If as an example of using a resonant acoustic mixer's the Resodyn ®, by periodic linear displacement of the container filling the mixture and supplying the acoustic energy, and using a plurality of mechanical or electronic transducer arrangement for this purpose, and more specifically And oscillator drives for transferring vibration and acceleration to the container and a flexible elastic member such as a spring.
  • the contents of the above resonance acoustic mixer can be found in U.S. Patent No. 7188993 and U.S. Patent Publication No. 2010-0294113.
  • the resonant mixing can be performed for 30 seconds to 30 minutes, specifically for a short time of 1 minute to 10 minutes. If the resonance mixing time is less than 30 seconds, it may be less mixed or the coating property may not be confirmed, and if it exceeds 30 minutes, the sample or composition may be changed.
  • the catalyst may further include a step of heat-treating any one selected from the group consisting of phthalocyanine, M-phthalocyanine and a mixture thereof to form a carbon coating layer containing carbon doped with the hetero element .
  • any one selected from the group consisting of phthalocyanine, M-phthalocyanine, and mixtures thereof may be selected from the group consisting of carbon nanofibers, carbon nanotubes, and mixtures thereof in all or part of the carbon coating layer Can be grown.
  • FIG. 4 is a diagram schematically showing an overall process procedure according to the method for producing the catalyst.
  • a coating layer 3 containing any one selected from the group consisting of phthalocyanine, M-phthalocyanine, and a mixture thereof is formed on the surface of the metal particles 2 and the support 1. Thereafter, heat treatment is performed on any one selected from the group consisting of phthalocyanine, M-phthalocyanine, and mixtures thereof to form a carbon coating layer 4 containing carbon doped with a hetero element. At this time, the phthalocyanine, M-phthalocyanine, or a mixture thereof, a carbon nanotube, a carbon nanotube, or a mixture thereof may be added to all or part of the carbon coating layer (4) ). ≪ / RTI >
  • the coating layer containing any one selected from the group consisting of phthalocyanine, M-phthalocyanine, and mixtures thereof is subjected to heat treatment to convert any one selected from the group consisting of phthalocyanine, M-phthalocyanine, To convert to carbon.
  • a carbon coating layer containing carbon doped with the hetero-element can be formed on the carrier and the metal particles supported thereon with a strong binding force, and the carbon nanofibers , Carbon nanotubes, and mixtures thereof.
  • the carbon nanofibers, the carbon nanotubes, and the mixture thereof may be three-dimensionally grown according to any one kind, content, and post-treatment condition selected from the group consisting of phthalocyanine, M- phthalocyanine, Can be grown, and the mass transfer capability and performance of the catalyst can be improved.
  • the coating thickness of the coating layer and the thickness of the carbon nanotube, the carbon nanotube, and the carbon nanotube may be changed by changing the kind, content, heat treatment temperature, heat treatment time and heat treatment atmosphere of any one selected from the group consisting of phthalocyanine, M- And mixtures thereof.
  • the length, diameter, and structure of any one of them can be controlled.
  • the heat treatment may be performed in an atmosphere of an inert gas or a reducing gas.
  • the inert gas may be any one selected from the group consisting of nitrogen, helium, argon, neon, krypton, xenon, radon, and mixed gas thereof.
  • the reducing gas may be a hydrogen mixed gas.
  • the heat treatment may be performed in an argon atmosphere or an argon-hydrogen mixed atmosphere.
  • a reduced form of the transition metal or an oxide type hetero particle may be partially doped to the carbon, And may be in the form of a metal alloy adjacent to the metal particles.
  • the argon-hydrogen mixed gas may have a hydrogen content of 2 vol% to 20 vol%, and more preferably 5 vol% to 15 vol%, based on the total volume of the mixed gas.
  • the hydrogen content is less than 2 vol% based on the total volume of the argon-hydrogen mixed gas, growth of any one selected from the group consisting of carbon nanofibers, carbon nanotubes, and mixtures thereof is inhibited or reduction of the transition metal And if it exceeds 20% by weight, there is a problem of deterioration of performance due to loss of existing catalyst such as growth of metal particles, loss of carrier, etc., and there is a risk of fire and explosion in the process .
  • the heat treatment may be carried out at a temperature of 400 ° C to 800 ° C, and specifically at a temperature of 500 ° C to 700 ° C. If the heat treatment temperature is lower than 400 ° C., the stability of the carbonized carbon may be deteriorated. If the heat treatment temperature is higher than 800 ° C., the catalytic activity may be lowered due to growth of metal particles or the like.
  • the heat treatment may be performed for 5 minutes to 60 minutes, specifically 5 minutes to 30 minutes, and more specifically 10 minutes to 40 minutes. When the heat treatment is performed for less than 5 minutes, the heat treatment effect may not be obtained. When the heat treatment is performed for more than 60 minutes, growth of the metal particles and any one of carbon nanofibers, carbon nanotubes, The activity of the catalyst due to excessive growth may be lowered.
  • An electrode according to another embodiment of the present invention includes the catalyst and an ionomer mixed with the catalyst.
  • the ionomer may be a cation conductor having a cation exchange group such as a proton, or an anion conductor having an anion exchange group such as a hydroxide ion, a carbonate or a bicarbonate.
  • the cation exchange group may be any one selected from the group consisting of a sulfonic acid group, a carboxyl group, a boronic acid group, a phosphoric acid group, an imide group, a sulfonimide group, a sulfonamide group and a combination thereof.
  • the cationic exchange group may be a sulfonic acid group or a carboxyl group have.
  • the cation conductor includes the cation-exchange group, and the fluorine-based polymer includes fluorine in the main chain; Polyimides, polyacetals, polyethylenes, polypropylenes, acrylic resins, polyesters, polysulfones, polyethers, polyetherimides, polyesters, polyethersulfones, polyetherimides, polyamides, polyamides, Hydrocarbon polymers such as carbonates, polystyrene, polyphenylene sulfide, polyether ether ketone, polyether ketone, polyaryl ether sulfone, polyphosphazene or polyphenylquinoxaline; Partially fluorinated polymers such as polystyrene-graft-ethylene tetrafluoroethylene copolymer, or polystyrene-graft-polytetrafluoroethylene copolymer; Sulfonimide, and the like.
  • the polymer may include a cation exchanger selected from the group consisting of a sulfonic acid group, a carboxylic acid group, a phosphoric acid group, a phosphonic acid group and derivatives thereof in the side chain, Specific examples include poly (perfluorosulfonic acid), poly (perfluorocarboxylic acid), copolymers of tetrafluoroethylene and fluorovinyl ethers containing sulfonic acid groups, defluorinated sulfated polyether ketone, or mixtures thereof
  • a fluorine-based polymer including; Sulfonated polyimide (S-PI), sulfonated polyarylethersulfone (S-PAES), sulfonated polyetheretherketone (SPEEK), sulfonated polybenzyl ether A sulfonated polybenzimidazole (SPBI), a sulfonated polybenzimidazole (SPBI), a sulf
  • the cation conductor may also be substituted with Na, K, Li, Cs or tetrabutylammonium in the cation exchange group at the side chain terminal.
  • H is replaced with Na in the cation exchange group at the side chain terminal
  • NaOH is substituted for tetrabutylammonium in place of tetrabutylammonium hydroxide
  • K, Li or Cs Can be substituted using appropriate compounds. Since the above-described replacement method is well known in the art, detailed description thereof will be omitted herein.
  • the cation conductor may be used singly or in the form of a mixture, and may also optionally be used together with a nonconductive compound for the purpose of further improving the adhesion with the ion exchange membrane. It is preferable to adjust the amount thereof to suit the purpose of use.
  • nonconductive compound examples include polytetrafluoroethylene (PTFE), tetrafluoroethylene-hexafluoropropylene copolymer (FEP), tetrafluoroethylene-perfluoroalkyl vinyl ether copolymer (PFA), ethylene / tetrafluoro (PVdF-HFP), dodecyltrimethoxysilane (DMSO), ethylene tetrafluoroethylene (ETFE), ethylene chlorotrifluoroethylene copolymer (ECTFE), polyvinylidene fluoride, polyvinylidene fluoride-hexafluoropropylene copolymer At least one selected from the group consisting of benzene sulfonic acid and sorbitol can be used.
  • PTFE polytetrafluoroethylene
  • FEP tetrafluoroethylene-hexafluoropropylene copolymer
  • PFA tetrafluoroethylene-perflu
  • the anionic conductor is a polymer capable of transporting an anion such as a hydroxy ion, a carbonate or a bicarbonate, and an anion conductor is commercially available in the form of a hydroxide or a halide (generally chloride) water purification, metal separation or carbon structure processes.
  • an anion conductor is commercially available in the form of a hydroxide or a halide (generally chloride) water purification, metal separation or carbon structure processes.
  • a metal hydroxide-doped polymer may be used as the anion conductor.
  • metal hydroxide doped poly ether sulfone
  • polystyrene vinyl polymer
  • poly (vinyl chloride) poly (vinylidene fluoride)
  • Poly tetrafluoroethylene
  • poly (benzimidazole) poly (ethylene glycol), and the like.
  • ionomer examples include naphion and acubion.
  • the ionomer may be contained in an amount of 20 to 45% by weight based on the total weight of the electrode, and may be specifically included in an amount of 25 to 38% by weight. If the content of the ionomer is less than 20% by weight, the performance of the fuel cell may be deteriorated. If the content of the ionomer is more than 45% by weight, excessive aggregation of the ionomer may occur.
  • the method for preparing the electrode includes preparing an electrode-forming composition including the catalyst and the ionomer, and coating the electrode-forming composition to prepare an electrode.
  • composition for forming an electrode including the catalyst and the ionomer is prepared.
  • the composition for forming an electrode may be prepared by adding the catalyst and the ionomer to a solvent and then subjecting the mixture to any one of dispersion methods selected from ultrasonic dispersion, stirring, 3-roll milling, oily stirring, high pressure dispersion, .
  • the catalyst may be dispersed in a wetting solution and then mixed with the ionomer or may be added to the ionomer in a solid state.
  • the solvent may be a solvent selected from the group consisting of water, a hydrophilic solvent, an organic solvent, and a mixture of at least one of them.
  • hydrophilic solvent is selected from the group consisting of alcohols, ketones, aldehydes, carbonates, carboxylates, carboxylic acids, ethers and amides containing linear or branched saturated or unsaturated hydrocarbons having 1 to 12 carbon atoms as a main chain Or more, and they may contain an alicyclic or aromatic cyclic compound as at least a part of the main chain.
  • the alcohol include methanol, ethanol, isopropyl alcohol, ethoxy ethanol, n-propyl alcohol, butyl alcohol, 1,2-propanediol, 1-pentanol, 1.5-pentanediol and 1,9-nonanediol; Ketones include heptanone, octanone and the like; Aldehydes include benzaldehyde, tolualdehyde and the like; Esters include methylpentanoate, ethyl-2-hydroxypropanoate and the like; Carboxylic acids include pentanoic acid, heptanoic acid and the like; Ethers include methoxybenzene, dimethoxypropane and the like; Amides include propanamide, butylamide, dimethylacetamide, and the like.
  • the organic solvent may be selected from N-methylpyrrolidone, dimethylsulfoxide, tetrahydrofuran, and mixtures thereof.
  • the solvent may be contained in an amount of 80% by weight to 95% by weight based on the total weight of the electrode forming composition. If the amount is less than 80% by weight, the solids content may be too high to cause dispersion problems due to cracking and high viscosity If it exceeds 95% by weight, the electrode activity may be deteriorated.
  • an electrode is prepared by coating the electrode forming composition.
  • the step of preparing the electrode may further include, for example, coating an electrode-forming composition on the release film to produce an electrode, and transferring the electrode to the ion exchange membrane.
  • the composition for electrode formation in which the active material is dispersed is continuously or intermittently transferred to a coater, and uniformly coated on the release film with a dry thickness of 1 to 200 ⁇ It is preferable to apply it.
  • the electrode-forming composition is continuously transferred through a pump to a coater such as a die, a gravure, a bar, a comma coater or the like according to the viscosity of the electrode-forming composition
  • the thickness of the electrode layer may be uniformly set to a dry thickness of 1 ⁇ ⁇ to 200 ⁇ ⁇ , more preferably 3 ⁇ ⁇ to 20 ⁇ ⁇ , on the decal film by a method such as coating, bar coating, comma coating, screen printing, spray coating, doctor blade coating, brush, And the solvent is volatilized by passing through a drying furnace maintained at a constant temperature.
  • the activity of the catalyst may be decreased due to a small amount of catalyst.
  • the coating is applied to a thickness exceeding 200 ⁇ , the distance of movement of ions and electrons increases, have.
  • the drying step may be a drying at 25 ° C to 90 ° C for 12 hours or more. If the drying temperature is less than 25 ° C. and the drying time is less than 12 hours, a problem may occur that a sufficiently dried electrode may not be formed. If the drying temperature is more than 90 ° C., cracking of the electrode may occur .
  • the method for applying and drying the electrode forming composition is not limited to the above.
  • the step of drying the electrode forming composition to form an electrode may further include a step of cutting the dried electrode and the release film to a desired size and bonding the electrode and the ion-exchange membrane.
  • the ion exchange membrane includes an ion conductor.
  • the ion conductor may be a cation conductor having a cation exchange group such as a proton, or an anion conductor having an anion exchange group such as a hydroxide ion, a carbonate or a bicarbonate. Since the description of the cation conductor and the anion conductor is the same as that described in the ionomer, repetitive description thereof will be omitted.
  • the ion exchange membrane may be a fluorine porous support such as e-PTFE or a reinforced membrane filled with a pore of a porous nano web support manufactured by electrospinning or the like.
  • a transfer method may be used.
  • the transfer method may be carried out at a temperature of 80 ⁇ to 150 ⁇ and 50 kgf / cm 2 to 200 kgf / cm 2 . If the hot-pressing is performed at 80 DEG C and less than 50 kgf / cm < 2 >, the transfer of the electrode on the release film may not be performed properly. If the temperature is higher than 150 DEG C, Structural modification may occur. When hot pressing is performed under the condition of exceeding 200 kgf / cm 2 , the effect of pressing the electrode is greater than that of the electrode, so that the transfer may not be performed properly.
  • the membrane-electrode assembly includes an anode electrode and a cathode electrode positioned opposite to each other, and the ion exchange membrane disposed between the anode electrode and the cathode electrode. Any one selected from the group consisting of the anode electrode, the cathode electrode, and both may include the electrode according to one embodiment of the present invention.
  • the membrane-electrode assembly 100 includes the electrodes 20 and 20 'disposed on both sides of the ion exchange membrane 50 and the ion exchange membrane 50, respectively.
  • the electrodes 20 and 20 ' include electrode substrates 40 and 40' and catalyst layers 30 and 30 'formed on the surfaces of the electrode substrates 40 and 40'
  • a microporous layer (not shown) containing conductive fine particles such as carbon powder and carbon black is formed between the catalyst layers 30 and 30 'so as to facilitate diffusion of the substances in the electrode base materials 40 and 40' .
  • an oxidation reaction which is disposed on one surface of the ion exchange membrane 50 to generate hydrogen ions and electrons from the fuel passed through the electrode substrate 40 to the catalyst layer 30,
  • the catalyst layer 30 ' is disposed on the other surface of the ion exchange membrane 50 and passes hydrogen ions supplied through the ion exchange membrane 50 and the electrode substrate 40'
  • the electrode 20 'causing the reduction reaction to generate water from the oxidant transferred to the cathode 20 is referred to as a cathode electrode.
  • a porous conductive base material may be used as the electrode base material 40 or 40 'so that hydrogen or oxygen can be supplied smoothly.
  • a metal film is formed on the surface of a cloth formed of a porous film or polymer fiber composed of carbon paper, carbon cloth, carbon felt or metal cloth ) May be used, but the present invention is not limited thereto.
  • the electrode substrate 40, 40 ' is water repellent with a fluorine-based resin, because the efficiency of diffusion of the reactant by the water generated during the operation of the fuel cell can be prevented from being lowered.
  • fluorine-based resin examples include polytetrafluoroethylene, polyvinylidene fluoride, polyhexafluoropropylene, polyperfluoroalkyl vinyl ether, polyperfluorosulfonyl fluoride alkoxyvinyl ether, fluorinated ethylene propylene ( Fluorinated ethylene propylene), polychlorotrifluoroethylene, or copolymers thereof.
  • the membrane-electrode assembly 100 may be fabricated according to a conventional method for manufacturing a membrane-electrode assembly, except that the electrode according to an embodiment of the present invention is used as the anode or cathode electrode 20, 20 ' .
  • a fuel cell according to another embodiment of the present invention includes the membrane-electrode assembly.
  • FIG. 6 is a schematic diagram showing the overall configuration of the fuel cell.
  • the fuel cell 200 includes a fuel supply unit 210 for supplying mixed fuel in which fuel and water are mixed, a reforming unit for reforming the mixed fuel to generate a reformed gas containing hydrogen gas A stack 230 for generating an electric energy by generating an electrochemical reaction with a reforming gas containing hydrogen gas supplied from the reforming unit 220 with an oxidizing agent and a stack 230 for oxidizing the oxidizing agent to the reforming unit 220 and the stack 220.
  • an oxidizing agent supply unit 240 supplying the oxidizing agent to the anode 230.
  • the stack 230 includes a plurality of unit cells for generating an electric energy by inducing an oxidation / reduction reaction of a reforming gas containing hydrogen gas supplied from the reforming unit 220 and an oxidizing agent supplied from the oxidizing agent supplying unit 240 Respectively.
  • Each of the unit cells refers to a cell that generates electricity.
  • the unit cell includes a reforming gas containing hydrogen gas and the membrane-electrode assembly for oxidizing / reducing oxygen in the oxidizing agent, a reforming gas containing hydrogen gas and an oxidizing agent (Or bipolar plate, hereinafter referred to as a separator plate) for supplying the membrane-electrode assembly to the membrane-electrode assembly.
  • the separator is disposed on both sides of the membrane-electrode assembly with the center thereof as the center. At this time, the separator located on the outermost side of the stack may be referred to as an end plate.
  • the end plate of the separation plate is provided with a pipe-shaped first supply pipe (231) for injecting a reformed gas containing hydrogen gas supplied from the reforming unit (220), and a pipe-shaped second supply pipe A first discharge pipe 233 for discharging the reformed gas containing hydrogen gas remaining unreacted in the plurality of unit cells to the outside, And a second exhaust pipe 234 for discharging the remaining oxidizing agent to the outside.
  • a pipe-shaped first supply pipe (231) for injecting a reformed gas containing hydrogen gas supplied from the reforming unit (220)
  • a pipe-shaped second supply pipe A first discharge pipe 233 for discharging the reformed gas containing hydrogen gas remaining unreacted in the plurality of unit cells to the outside
  • a second exhaust pipe 234 for discharging the remaining oxidizing agent to the outside.
  • the electrode is applicable to various fields such as a secondary cell or a capacitor in addition to the membrane-electrode assembly for a fuel cell.
  • the catalyst prepared in Example 1 was spread on an alumina boat, and the alumina boat containing the sample was placed in a heating furnace with rails. While the furnace was purged with argon gas, the temperature of the furnace was set to 600 ° C, and then the temperature was raised. When the set temperature was reached, the heating furnace was moved to the portion where the sample was present, and heat was applied to the sample for 30 minutes. After the elapse of the set time, the heating furnace was moved to the original position from the portion where the sample was present, and the catalyst was recovered after the heating furnace was completely cooled.
  • the catalyst prepared in Example 1 was spread on an alumina boat, and the alumina boat containing the sample was placed in a heating furnace with rails. While the furnace was purged with argon gas, the temperature of the furnace was set to 600 ° C, and then the temperature was raised. At the set temperature, an argon-hydrogen mixed gas (containing 10 vol% hydrogen) was flowed. The heating furnace was moved to the portion where the specimen was present, and heat was applied to the specimen for 30 minutes. After the elapse of the set time, the heating furnace was moved to the original position from the portion where the sample was present, and the catalyst was recovered after the heating furnace was completely cooled.
  • argon-hydrogen mixed gas containing 10 vol% hydrogen
  • Co-phthalocyanine was spread on an alumina boat, and the alumina boat containing the sample was placed in a heating furnace with rails. While the furnace was purged with argon gas, the temperature of the furnace was set to 600 ° C, and then the temperature was raised. When the set temperature was reached, the heating furnace was moved to the portion where the sample was present, and heat was applied to the sample for 30 minutes. After the elapse of the set time, the heating furnace was moved to the original position from the portion where the sample was present, and the catalyst was recovered after the heating furnace was completely cooled.
  • Co-phthalocyanine was spread on an alumina boat, and the alumina boat containing the sample was placed in a heating furnace with rails. While the furnace was purged with argon gas, the temperature of the furnace was set to 600 ° C, and then the temperature was raised. At the set temperature, an argon-hydrogen mixed gas (containing 10 vol% hydrogen) was flowed. The heating furnace was moved to the portion where the specimen was present, and heat was applied to the specimen for 30 minutes. After the elapse of the set time, the heating furnace was moved to the original position from the portion where the sample was present, and the catalyst was recovered after the heating furnace was completely cooled.
  • argon-hydrogen mixed gas containing 10 vol% hydrogen
  • a simple mixture of 1.0 g of a commercial Pt / C catalyst and 0.1 g of Co-phthalocyanine was spread on an alumina boat, and the alumina boat containing the sample was placed in a heating furnace with rails. While the furnace was purged with argon gas, the temperature of the furnace was set to 600 ° C, and then the temperature was raised. When the set temperature was reached, the heating furnace was moved to the portion where the sample was present, and heat was applied to the sample for 30 minutes. After the elapse of the set time, the heating furnace was moved to the original position from the portion where the sample was present, and the catalyst was recovered after the heating furnace was completely cooled.
  • a simple mixture of 1.0 g of a commercial Pt / C catalyst and 0.1 g of Co-phthalocyanine was spread on an alumina boat, and the alumina boat containing the sample was placed in a heating furnace with rails. While the furnace was purged with argon gas, the temperature of the furnace was set to 600 ° C, and then the temperature was raised. At the set temperature, an argon-hydrogen mixed gas (containing 10 vol% hydrogen) was flowed. The heating furnace was moved to the portion where the specimen was present, and heat was applied to the specimen for 30 minutes. After the elapse of the set time, the heating furnace was moved to the original position from the portion where the sample was present, and the catalyst was recovered after the heating furnace was completely cooled.
  • argon-hydrogen mixed gas containing 10 vol% hydrogen
  • 0.1 g of a 20 wt% Pt / C (HISPEC, A Johnson Matthey company) catalyst was mixed with 100 ml of an aqueous solution of ethylenediamine, followed by reflux stirring at 75 ⁇ for 8 hours. Then, the suspension containing the catalyst and the aqueous solution of ethylenediamine was rinsed with distilled water and ethanol using a reduced pressure filtration apparatus, filtered, and then dried in an oven at 60 ° C for 8 hours. Then, the powdery catalyst was recovered. The dried catalyst was heat treated in a heating furnace of argon gas atmosphere for 2 hours to prepare a Pt / C catalyst (ED treated 20% Pt / C) having a 1 nm thick protective layer containing nitrogen-doped carbonaceous material.
  • a 20 wt% Pt / C (HISPEC, A Johnson Matthey company) catalyst was mixed with 100 ml of an aqueous solution of ethylenediamine, followed by reflux stirring at 75 ⁇ for 8 hours. Then, the
  • a catalyst was prepared in the same manner as in Example 1 except that the carbon support was coated with Co-phthalocyanine in Example 1, and Pt was supported on the Co-coated phthalocyanine-coated carbon support to prepare a catalyst. Respectively.
  • FIG. 7 shows the result of Co-phthalocyanine coating of the TEC10E50E product of Tanaka Co., Ltd. in Example 1
  • FIG. 8 shows Co-phthalocyanine coating the high durability carrier in the same manner as in Example 1.
  • Co-phthalocyanine is uniformly coated on the surface of the Pt / C catalyst with a small thickness. Also, referring to FIG. 8, Co-phthalocyanine can be easily coated by using the method of the present invention for other catalysts using a high-durability carrier.
  • TEM 9 is a transmission electron microscope (TEM) photograph of a product of TANKAE TEC10E50E used in Example 1
  • Fig. 10 is a transmission electron microscope (TEM) photograph of the catalyst prepared in Example 3.
  • a carbonized coating layer containing carbon in which the Co-phthalocyanine is carbonized and doped with a hetero element is formed, and at the same time, a carbon nano- Fiber, carbon nanotube, and a mixture thereof.
  • a scanning electron microscope (SEM) photograph of the catalyst prepared in the argon atmosphere prepared in Example 2 and a scanning electron microscope (SEM) photograph of the catalyst prepared in the argon-hydrogen mixed gas atmosphere prepared in Example 3 are shown in Figs. 11 and 12, respectively.
  • any one selected from the group consisting of carbon nanofibers, carbon nanotubes, and mixtures thereof formed on the entire surface or a part of the surface of the carbon coating layer containing the hetero-element-doped carbon is argon - hydrogen mixed gas, the diameter is larger, and the shape is long and distinct.
  • the catalyst prepared in the above Examples and Comparative Examples was added to a solution prepared by mixing an ionomer and isopropanol, and subjected to ultrasonic treatment to prepare a composition for electrode formation.
  • composition for electrode formation was coated on a rotating disk electrode made of gycarbons and dried to prepare a working electrode (active area: 0.196 cm 2 ).
  • the electrochemical characteristics of the working electrode, the Ag / AgCl electrode as the reference electrode, and the electrochemical measurement device using the platinum wire as the counter electrode were analyzed in a 1 M HClO 4 electrolyte solution.
  • the cyclic voltammetry (CV) cycle was performed for 10,000 cycles using each catalyst prepared above. At this time, the rate of change of the catalytic active area before and after the cycle was measured, and the results are shown in Table 1 and FIG.
  • the durability of the catalyst is improved through the fact that the catalysts prepared in the above Examples have a smaller area reduction rate of catalyst activity after 10,000 cycles than the Comparative Example 1 (commercial catalyst)
  • the coating layer containing Co-phthalocyanine is not only increased in durability but also significantly improved in durability after heat treatment as in Examples 2 and 3.
  • the catalysts prepared in the above-mentioned Examples show larger active areas of the initial catalysts than the catalysts prepared in the above Comparative Examples.
  • Example 3 The durability of the catalyst was evaluated through comparison of catalytic active areas after 10,000 CV cycles, and as a result, the durability of the catalyst was evaluated in the order of Example 3> Example 2> Comparative Example 5> Comparative Example 4> Comparative Example 6> Increased results were obtained.
  • the catalytic activity may be lowered due to the desorption, growth, or the like of the metal particles during the ethylenediamine treatment
  • the carbon coating layer does not include any one selected from the group consisting of carbon nanofibers, carbon nanotubes, and mixtures thereof on the whole or part of the surface of the carbon coating layer as in the present invention. do.
  • a commercially available Pt / C catalyst (commercial catalyst) and the catalyst prepared in Example 3 (CoPc) were added to a solution prepared by mixing an ionomer and isopropanol and ultrasonicated to prepare a composition for electrode formation.
  • the catalyst (CoPc) prepared in the above example was mixed at 0 wt%, 20 wt% and 10 wt%, respectively.
  • composition for electrode formation was coated on a rotating disk electrode made of gycarbons and dried to prepare a working electrode (active area: 0.196 cm 2 ).
  • the electrochemical characteristics of the working electrode, the Ag / AgCl electrode as the reference electrode, and the electrochemical measurement device using the platinum wire as the counter electrode were analyzed in a 1 M HClO 4 electrolyte solution.
  • the catalyst slurry composition was applied to a polyimide release film at a coating rate of 10 mm / s and a coating thickness of 100 ⁇ , and dried at 30 ⁇ for 6 hours to prepare an electrode.
  • the dried electrode was cut to a required size, and the electrode surface and the electrolyte membrane were aligned on both sides of a polymer electrolyte membrane (manufactured by Du Pont Company; Nafion 212 Membrane). Pressed for minutes, maintained at room temperature for 1 minute, hot-pressed and transferred, and the release film was peeled to prepare a membrane-electrode assembly.
  • a polymer electrolyte membrane manufactured by Du Pont Company; Nafion 212 Membrane
  • the initial performance of the prepared membrane-electrode assembly was measured after supplying the fuel with a fixed flow rate of 0.6 V standard and activating the cycle in which the voltage was changed in the OCV 0.3 V range at 65 ° C and atmospheric pressure. The results are shown in Table 2 below.
  • CV Cyclovoltammetry
  • Example 3 the durability of the catalyst was evaluated by comparing the catalytic active areas after 20,000 CV cycles. As a result, it was found that about 11% in Example 3, about 45% in Example 1, And a performance reduction of about 57%. Thus, the results of Example 3 and Example 1 were superior to those of Comparative Example 7.
  • a coating layer comprising any one selected from the group consisting of phthalocyanine, M-phthalocyanine, and mixtures thereof
  • Second discharge pipe 240 Oxidizing agent supply part
  • the present invention relates to a catalyst, a method for producing the same, an electrode, a membrane-electrode assembly and a fuel cell comprising the same, wherein the catalyst forms a coating layer on the surface of a catalyst through a comparatively easy method,
  • the durability is improved and the catalyst including the coating layer is post-treated to form a carbon coating layer. Further, durability is further improved, and the carbon nanofibers or carbon nanotubes produced during the post-treatment process have improved mass transfer performance and performance will be.

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Abstract

La présente invention concerne un catalyseur, son procédé de préparation, une électrode le comprenant, un ensemble membrane-électrode et une pile à combustible, le catalyseur comprenant : un support ; des particules métalliques prises en charge par le support ; et une couche de revêtement située sur les particules métalliques, et comprenant un élément quelconque choisi dans le groupe constitué par la phtalocyanine, la M-phtalocyanine (où M est un métal de transition) et un mélange des deux. Le catalyseur présente une durabilité améliorée étant donné qu'une couche de revêtement est formée sur la surface d'un catalyseur commercial ou d'un catalyseur classique par l'intermédiaire d'un procédé relativement facile sans traitement séparé, la durabilité est davantage améliorée étant donné qu'une couche de revêtement de carbone est formée par post-traitement d'un catalyseur comprenant la couche de revêtement, et la capacité ainsi que la performance de transfert de matériau sont également améliorées par une nanofibre de carbone ou un nanotube de carbone générés pendant le post-traitement.
PCT/KR2018/015195 2017-12-26 2018-12-03 Catalyseur, son procédé de préparation, électrode le comprenant, ensemble membrane-électrode et pile à combustible Ceased WO2019132281A1 (fr)

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EP18893847.6A EP3734728A4 (fr) 2017-12-26 2018-12-03 Catalyseur, son procédé de préparation, électrode le comprenant, ensemble membrane-électrode et pile à combustible
US16/957,530 US11831025B2 (en) 2017-12-26 2018-12-03 Catalyst, preparation method therefor, electrode comprising same, membrane-electrode assembly, and fuel cell
JP2020532966A JP2021506573A (ja) 2017-12-26 2018-12-03 触媒、その製造方法、これを含む電極、膜−電極アセンブリー及び燃料電池
CN201880083886.7A CN111527633B (zh) 2017-12-26 2018-12-03 催化剂、其制备方法、包含所述催化剂的电极、膜-电极组件和燃料电池

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JP2021161154A (ja) * 2020-03-30 2021-10-11 旭化成株式会社 アイオノマー
JP2022041027A (ja) * 2020-08-31 2022-03-11 シャープ株式会社 触媒、触媒の製造方法、空気極、および空気電池
JP2023500468A (ja) * 2020-05-28 2023-01-06 コーロン インダストリーズ インク 燃料電池用混合触媒、その製造方法、それを用いた電極形成方法、及びそれを含む膜電極アセンブリー
WO2023101309A1 (fr) * 2021-11-30 2023-06-08 코오롱인더스트리 주식회사 Catalyseur pour pile à combustible, son procédé de préparation, couche catalytique le comprenant, ensemble membrane-électrode et pile à combustible

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