WO2004036673A1 - 燃料電池用電極と電解質複合体およびそれらの製造方法 - Google Patents
燃料電池用電極と電解質複合体およびそれらの製造方法 Download PDFInfo
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- WO2004036673A1 WO2004036673A1 PCT/JP2003/013449 JP0313449W WO2004036673A1 WO 2004036673 A1 WO2004036673 A1 WO 2004036673A1 JP 0313449 W JP0313449 W JP 0313449W WO 2004036673 A1 WO2004036673 A1 WO 2004036673A1
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- WIPO (PCT)
- Prior art keywords
- resin
- fuel cell
- electrode
- electrodes
- coating
- Prior art date
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Classifications
-
- 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
- H01M4/88—Processes of manufacture
- H01M4/8878—Treatment steps after deposition of the catalytic active composition or after shaping of the electrode being free-standing body
- H01M4/8882—Heat treatment, e.g. drying, baking
-
- 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
- H01M4/88—Processes of manufacture
- H01M4/8825—Methods for deposition of the catalytic active composition
-
- 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]
-
- 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
- H01M4/8605—Porous electrodes
-
- 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
- Electrode and electrolyte composite for fuel cell and method for producing them are Electrode and electrolyte composite for fuel cell and method for producing them
- the present invention relates to a fuel cell electrode, a method for producing the same, a polymer electrolyte membrane, and a fuel cell electrolyte composite comprising a pair of electrodes joined to each other with a catalyst interposed on both sides of the electrolyte membrane. It relates to the manufacturing method. Background art
- a single cell of a fuel cell is composed of, for example, an electrolyte membrane made of a fluororesin-based ion exchange membrane, and a pair of electrodes joined to both sides of the electrolyte membrane with a catalyst interposed therebetween.
- a gas flow path for supplying oxygen and hydrogen gas is provided.
- the electrolyte membrane is extremely thin and is not self-supporting, and the electrodes bonded to both surfaces are also made of carbon paper, etc., so that the electrolyte composite composed of the electrolyte membrane and a pair of electrodes also has self-sustainability. Absent.
- a self-supporting carbon separator is provided outside the two electrodes, and a groove for the gas flow path is formed on the inner surface of the separator so that the separator can be self-supporting with the electrolyte composite interposed therebetween.
- a groove for the gas flow path is formed on the inner surface of the separator so that the separator can be self-supporting with the electrolyte composite interposed therebetween.
- An object of the present invention is to provide a fuel cell electrode and an electrolyte composite that can be reduced in cost and thickness, and a method for producing the fuel cell electrode and the electrolyte composite. Disclosure of the invention
- a first characteristic configuration of the fuel cell electrode according to the present invention is that the electrode is composed of a porous thermoplastic resin having air permeability, and a metal supported on the thermoplastic resin in a three-dimensional matrix. .
- the fuel cell electrode is made of a porous thermoplastic resin having air permeability and a metal supported on the thermoplastic resin in a matrix in a three-dimensional direction. Energization is ensured by the metal in the shape, and the necessary conditions for the fuel cell electrode, that is, while having air permeability and electric conductivity, the self-sustainability by the thermoplastic resin is also provided.
- a second characteristic configuration of the fuel cell electrode according to the present invention is a fuel cell electrode having the above-described first characteristic configuration, wherein the thermoplastic resin is polytetrafluoroethylene (PTFE), polyethylene ( PE), polypropylene (PP), ABS resin, polyamide (PA), polysulfone (PSU), AS resin, polystyrene (PS), vinylidene chloride resin (PVDC), vinylidene fluoride resin, PFA resin At least one selected from the group consisting of polyphenylene ether (PFE), methylpentene resin, and methacrylic acid resin.
- the thermoplastic resin is polytetrafluoroethylene (PTFE), polyethylene ( PE), polypropylene (PP), ABS resin, polyamide (PA), polysulfone (PSU), AS resin, polystyrene (PS), vinylidene chloride resin (PVDC), vinylidene fluoride resin, PFA resin At least one selected from the group consisting of polyphenylene ether (PFE),
- the thermoplastic resin constituting the fuel cell electrode is made of polytetrafluoroethylene (PTFE), polyethylene (PE), polypropylene (PP), ABS resin, polyamide (PA), Polysulfone (PSU), AS resin, Polystyrene (PS), Vinylidene chloride resin (PVDC), Vinylidene fluoride resin, Since it is at least one selected from the group consisting of PFA resin, polyphenylene ether (PFE), methylpentene resin, and methacrylic acid resin, it has sufficient conditions necessary for fuel cell electrodes, It is desirable to have the necessary independence.
- PTFE polytetrafluoroethylene
- PE polyethylene
- PP polypropylene
- ABS resin polyamide
- PA Polysulfone
- PS Polystyrene
- PS Polystyrene
- PVDC Vinylidene chloride resin
- VDC Vinylidene fluoride resin
- a first characteristic configuration of the fuel cell electrolyte composite according to the present invention is a fuel cell electrolyte membrane comprising a polymer electrolyte membrane, and a pair of electrodes joined to both surfaces of the membrane with a catalyst interposed therebetween.
- An electrolyte composite, wherein each of the pair of electrodes is made of a porous thermoplastic resin having air permeability and a metal supported on the thermoplastic resin in a three-dimensional matrix. is there.
- each of the pair of electrodes joined to each other with the catalyst interposed therebetween on both surfaces of the polymer electrolyte membrane is formed of a porous thermoplastic resin having air permeability and the thermoplastic resin. Since it is made of a metal supported in a three-dimensional direction in a matrix, the energization of the electrode is ensured by the matrix-like metal, and the thermoplastic resin of the electrode is provided while satisfying the necessary conditions for the electrolyte composite for a fuel cell. As a result, the electrolyte composite itself becomes self-sustaining.
- the separator it is not particularly necessary to provide the separator with a self-supporting structure.For example, it is possible to form a groove for the gas flow passage in the electrode itself by press working. Thereby, the cost and thickness of the fuel cell can be reduced.
- the first characteristic means of the method for producing an electrode for a fuel cell according to the present invention is that a metal film is formed on the surface of a large number of particles made of a thermoplastic resin by plating, and a large number of particles formed by the metal film are formed. The point is that the body is pressurized and joined in a plate shape by pressing.
- a second aspect of the method for producing an electrode for a fuel cell according to the present invention is a method for producing an electrode for a fuel cell having the above first aspect, wherein the particle size of the powder is 0.1. m ⁇ l 0 0 ⁇ .
- the thermoplastic resin powder has a particle size of 0.1 ⁇ !
- the electrode has both the required air permeability and electrical conductivity.
- a third aspect of the method for manufacturing an electrode for a fuel cell according to the present invention is a method for manufacturing an electrode for a fuel cell having the above-described first or second aspect, wherein the metal film is a Ni film, a Ni film. Alloy coating, Ni-based composite coating, Cu coating, Cu-based alloy coating, Cu-based composite coating, Au coating, Pt coating, Pt-based alloy coating, Pd coating, Rh coating, and Ru This is one of a group of films.
- the metal film formed on the surface of the thermoplastic resin powder or granules is formed of a Ni film, a Ni-based alloy film, or a Ni-based composite film.
- a fourth aspect of the method for manufacturing a fuel cell electrode according to the present invention is a method for manufacturing an electrode for a fuel cell having the above-described first or second aspect, wherein the metal film is formed of Ni 1 P, N This is a film selected from the group consisting of i-B, Ni-Cu-P, Ni-Co-P, and Ni-Cu-B.
- the metal film formed on the surface of the thermoplastic resin powder or granules is Ni—P, Ni—B, Ni—Cu— Since it is a single film selected from the group consisting of P, Ni—Co—P, and Ni—Cu—B, it is desirable that the electrodes have the necessary electrical conductivity in this case as well.
- a fifth aspect of the method for producing an electrode for a fuel cell according to the present invention is a method for producing an electrode for a fuel cell having the above-mentioned first or second aspect, wherein, when forming the metal film, Fine particles other than the above are included in the metal film, and the fine particles are made of polytetrafluoroethylene (PTFE), polyethylene (PE), polypropylene (PP), ABS resin, polyamide (PA), polysulfone (P SU), AS resin, polystyrene (PS), polyvinylidene chloride resin (PVDC), vinylidene fluoride resin, PFA resin, polyphenylene ether (PFE), methylpentene resin, methacrylic acid resin, carbon ( C), selected from the group consisting of catalyst-supporting fine particles and thermosetting resin It is at least one thing.
- PTFE polytetrafluoroethylene
- PE polyethylene
- PP polypropylene
- ABS resin polyamide
- PA polysulfone
- PS polys
- a first characteristic means of the method for producing an electrolyte composite for a fuel cell according to the present invention comprises a solid polymer electrolyte membrane, and a pair of electrodes joined to both surfaces of the electrolyte membrane with a catalyst interposed therebetween.
- a method for producing an electrolyte composite for a fuel cell comprising forming a metal film on the surface of a large number of particles made of a thermoplastic resin by plating, and pressing the large number of particles formed with the metal film. To form the pair of electrodes by pressing and joining them in a plate shape, joining the electrolyte membranes with the catalyst interposed on one surface of each of the pair of electrodes, and joining the electrolyte membranes of both electrodes together. It is a point of manufacturing by joining.
- the surface of a large number of particles made of a thermoplastic resin may be damaged by plating. Since a metal film is formed and a large number of powders with the metal film are pressed and bonded to form a plate, they can be easily manufactured by relatively simple processing such as plating and pressure bonding.
- the electrolyte membranes are joined with a catalyst interposed on one side of each of the electrodes, and the electrolyte membranes of both electrodes are joined together.
- the electrolyte composite can be easily and easily manufactured.
- the second characteristic means of the method for producing an electrolyte composite for a fuel cell according to the present invention includes a solid polymer electrolyte membrane, and a pair of electrodes joined to each other with a catalyst interposed on both surfaces of the electrolyte membrane.
- a method for producing an electrolyte composite for a fuel cell comprising electrodes, comprising forming a metal film on a surface of a number of particles made of a thermoplastic resin by plating, and forming a number of particles formed by the metal film. Is press-bonded into a plate shape to produce the pair of electrodes, and the pair of electrodes is joined to a surface of the electrolyte membrane with the catalyst interposed therebetween.
- the surface of a large number of particles made of a thermoplastic resin may be damaged by plating. Since a metal film is formed and a large number of powders with the metal film formed are pressed and bonded into a plate shape and manufactured, the electrodes can be easily formed by relatively simple processing such as plating and pressure bonding.
- each of the electrodes is joined to both surfaces of an electrolyte membrane with a catalyst interposed therebetween, so that the electrolyte composite is produced. Simple and easy to manufacture.
- FIG. 1 is an explanatory diagram showing a production process of a fuel cell electrode and an electrolyte composite according to Example 1.
- FIG. 2 is a schematic diagram of a microscopically enlarged portion A in FIGS. 1 and 4.
- FIG. 3 is an explanatory view showing a single cell of the fuel cell according to Example 1,
- FIG. 4 is an explanatory diagram showing a production process of a fuel cell electrode and an electrolyte composite according to Example 2.
- FIG. 5 is an explanatory diagram showing a single cell of the fuel cell according to Embodiment 2,
- FIG. 6 is an explanatory view showing a process for producing a fuel cell electrode and an electrolyte composite according to another embodiment.
- a fuel cell electrode As shown in Fig. 3, one cell of the fuel cell is composed of a polymer electrolyte membrane 1 and catalysts 2 on both sides of the electrolyte membrane 1.
- a pair of electrodes 3 is joined with the electrodes interposed, and a pair of separators 4 is joined outside each electrode 3.
- the electrolyte composite according to the present invention comprises a solid polymer electrolyte membrane 1 and a pair of electrodes 3 bonded to both surfaces of the electrolyte membrane 1 with a catalyst 2 interposed therebetween.
- a granular material 3 a made of a thermoplastic resin It is composed of a conductive metal 3b supported in a three-dimensional matrix by the body 3a.
- each electrode 3 forms a metal 3b film on the surface of a thermoplastic resin powder 3a having a particle size of 0.1 m to 1 000 / m by plating, and forms the metal film.
- a large number of the formed granules 3a are manufactured by pressing and joining them in a plate shape by pressing, and the metal film of each granule 3a forms a matrix-shaped conductive metal 3b.
- the thermoplastic resin constituting each electrode 3 includes polytetrafluoroethylene (PTFE), polyethylene (PE), polypropylene (PP), ABS resin, polyamide (PA), polysulfone (PSU), AS resin, polystyrene (PS), vinylidene chloride resin (PVDC), vinylidene fluoride resin, PFA resin, polyphenylene ether (PFE), methylpentene resin, and at least one of the methacrylic acid resin groups One of them can be used.
- conductive metal 3b as described later, Ni,: Ni-based alloy, Cu, Cu-based alloy, Au, Pt, Pt-based alloy, You can use one of the groups Pd, Rh, and Ru.
- Example 1 Polytetrafluoroethylene (PTFE) is selected as the thermoplastic resin, and a PTFE-based surfactant with a mean particle size of 20; A surface conditioning treatment was performed. Specifically, the 0. 75 gZL [C 8 F 17 S 0 2 NH (CH 2) 3 (CH 3) 2 N +] I a PTFE granular material 7 0 ° C - was stirred in an aqueous solution for 10 minutes After that, it was thoroughly washed with water.
- PTFE polytetrafluoroethylene
- a cationic surfactant other than a fluorine-based surfactant, an anion surfactant, a nonionic surfactant, or the like can be used in addition to the fluorine-based surfactant.
- the PTFE powder after the surface treatment is activated twice by repeating the process of sensitizing with a sensitizer, sufficient washing with water, applying a catalyst with an activator, and sufficient washing with water twice. did.
- the activation of the catalyst on the surface can be performed by, for example, repeating the catalyst applying step and the activation treatment step using a thin acid, in addition to the above-described method.
- the Ni powder was subjected to electrolytic Ni plating on the PTFE powder using a plating device disclosed in Japanese Patent Application Laid-Open No. Hei 9-106817.
- the bath composition and conditions of the Ni plating solution are shown in Table 2 below. Table 2
- the substrate was sufficiently washed with water and dried under vacuum under reduced pressure for 1 hour.
- the plating amount was 65.2% by weight, and the average plating film thickness was 0.35 / m.
- Vacuum degassing of the Ni Mekki PTFE powder obtained in this manner was performed at 300 ° C, 10 OMPa for 5 minutes by a flat plate press using a mold with one side processed into a convex shape. While pressing, a molded article having a length of 4 Omm, a width of 40 mm, and a thickness of 1 mm was obtained on one side of an irregular shape and the other side was flat. Since this molded article was to be the base of the fuel cell electrode, its cross section was observed, and it was confirmed that the article was porous with air permeability.
- a portion of about 100 m on the flat side of the molded body was treated with thin nitric acid to dissolve the Ni plating film, and a platinum (Pt) catalyst was supported on the plating portion by an electrolytic plating method.
- An alcohol dispersion of naphion (a fluorine-based solid electrolyte resin provided with a sulfone group: manufactured by DuPont) serving as a polymer electrolyte membrane was applied and impregnated.
- 8 mg of the platinum catalyst was supported.
- Fig. 1 is a fluorinated solid electrolyte resin as a polymer electrolyte membrane
- 2 is a platinum catalyst
- 3a is an electrode.
- the PTFE powder as a thermoplastic resin constituting 3 and 3b as Ni as a metal constituting the electrode 3 had a total thickness of 1.2 mm and was self-supporting.
- a pair of the composites is prepared, and one side is a cathode and the other is an anode, and the surfaces on the electrolyte resin 1 side are bonded to each other and joined together, and a force of 0.5 mm is applied to the outside thereof.
- the single cell of the polymer electrolyte fuel cell shown in Fig. 3 was produced by crimping a single-bon separator 4.
- the thickness of this single cell is 3.4 mm, which makes it considerably thinner than the conventional single cell with a thickness of 5 rnm. For example, assuming a stack of 400 cells for electric vehicles, a stack that used to be 200 cm in the past can be reduced to about 13.6 cm.
- a voltage of 0.589 V can be taken out at 50 ° C.
- a voltage close to 0.6 V can be obtained even in an atmosphere of ° C.
- the electromotive force is greatly influenced by the moisturizing property of the anode surface, and when the hydrogen ions, which are the charge carriers, move from the anode to the force sword, the hydration water moves with it, but if the water on the anode side runs out, However, it will not be possible to extract any more voltage. Therefore, there is a high possibility that the electrode will not operate at a high temperature at which water evaporates easily.
- one surface of the electrode is etched by an acid treatment, so that the electrolyte membrane and The interface has a complicated structure, and the moisturizing effect of water has been improved, so operation at 90 ° C is possible.
- a Ni film is formed as a metal film on the surface of a granular material of a thermoplastic resin, but in addition to the Ni film, a Ni-based alloy film, a Ni-based composite film, Selected from the group consisting of Cu coating, Cu-based alloy coating, Cu-based composite coating, Au coating, Pt coating, Pt-based alloy coating, Pd coating, Rh coating, and Ru coating Only one skin It can be carried out by forming a film, and from the group of Ni-P, Ni-B, Ni-Cu-P, Ni-Co-P, Ni-Cu-B It can also be implemented by forming one selected film.
- PMMA Polymethyl methacrylate
- methacrylic acid resin an example of a methacrylic acid resin
- the average particle size was 10 m.
- the metal film was formed on the surface of the PMMA powder by performing the treatment and performing electroless Ni-PTFE plating. Table 4 below shows the bath composition and conditions of the Ni-PTFE plating solution.
- the Ni-PTFE plating PMMA powder obtained in this manner was mixed uniformly with calcium carbonate particles having an average particle size of 5 m to 5 parts by weight, and a mold processed into an uneven shape was prepared. Using a flat plate press at 400 ° C and 10 OMPa for 5 minutes under vacuum while depressurizing, pressurized to obtain a molded body with irregularities on both sides, length 40 mm, width 40 mm, thickness lmm was. Observation of the cross section of the molded body that was the base of this fuel cell electrode revealed that it was a dense plane, but when the molded body was treated with water containing a dilute acid to dissolve the calcium carbide, It was confirmed that the porous material had air permeability.
- naphion a fluorine-based solid electrolyte resin provided with a sulfone grave: DuPont
- naphion a fluorine-based solid electrolyte resin provided with a sulfone grave: DuPont
- the composite thus produced is shown in Fig. 4, where 1 is a fluorine-based solid electrolyte resin as a polymer electrolyte membrane, 2 is a platinum catalyst, 3 is an electrode, and the overall thickness was 1.3 mm, and was self-sustaining.
- the electrode 3 also has the form shown in Fig. 2 when enlarged microscopically, and the surface of the PMMA powder 3a as a thermoplastic resin is covered with Ni as metal 3b. It had been.
- a pair of the composites is prepared, and one side is used as a force source and the other is used as an anode, and the surfaces of the electrolyte resin 1 are bonded to each other and joined together, and a 0.5 mm-thick force separator is formed on the outside thereof.
- the single polymer fuel cell shown in Fig. 5 was manufactured by crimping 4.
- This single cell was 3.6 mm. Using this single cell, the electromotive force was measured in a constant temperature bath at 50 ° C to 90 ° C in the same manner as in Example 1. A voltage close to 0.6 V could be obtained even under the atmosphere of C.
- Example 2 a Ni-PTFE film was formed as a metal film on the surface of the granular material of the thermoplastic resin.
- PTFE polytetrafluoroethylene
- PE polyethylene
- PP polypropylene
- PA polyamide
- PSU polysulfone
- AS resin polystyrene
- PVDC polyvinylidene chloride resin
- VDC vinylidene fluoride resin
- PFA polyphenylene ether
- C methacrylic acid resin
- catalyst support It can be carried out by including at least one fine particle selected from the group consisting of fine particles and a thermosetting resin.
- the bonding of the separator 4 to each electrode 3 can be performed before or after the bonding of the electrode 3 to the electrolyte membrane 1.
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- Electrochemistry (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Thermal Sciences (AREA)
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- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Inert Electrodes (AREA)
- Fuel Cell (AREA)
Abstract
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Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/532,010 US20060141336A1 (en) | 2002-10-21 | 2003-10-21 | Electrode and electrolyte composite for fuel cell, and method for manufacture thereof |
AU2003273068A AU2003273068A1 (en) | 2002-10-21 | 2003-10-21 | Electrode and electrolyte composite for fuel cell, and method for manufacture thereof |
CA002503158A CA2503158A1 (en) | 2002-10-21 | 2003-10-21 | Electrode and electrolyte composite for fuel cell, and method for manufacture thereof |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2002-306153 | 2002-10-21 | ||
JP2002306153A JP4355822B2 (ja) | 2002-10-21 | 2002-10-21 | 燃料電池用電極と電解質複合体の製造方法 |
Publications (1)
Publication Number | Publication Date |
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WO2004036673A1 true WO2004036673A1 (ja) | 2004-04-29 |
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ID=32105194
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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PCT/JP2003/013449 WO2004036673A1 (ja) | 2002-10-21 | 2003-10-21 | 燃料電池用電極と電解質複合体およびそれらの製造方法 |
Country Status (5)
Country | Link |
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US (1) | US20060141336A1 (ja) |
JP (1) | JP4355822B2 (ja) |
AU (1) | AU2003273068A1 (ja) |
CA (1) | CA2503158A1 (ja) |
WO (1) | WO2004036673A1 (ja) |
Families Citing this family (2)
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JP4882541B2 (ja) * | 2006-06-26 | 2012-02-22 | トヨタ自動車株式会社 | 燃料電池用電解質膜および膜電極接合体の製造方法 |
KR100957302B1 (ko) | 2007-09-07 | 2010-05-12 | 현대자동차주식회사 | 연료전지용 막-전극 접합체의 제조방법 |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6229069A (ja) * | 1985-07-30 | 1987-02-07 | Masahiro Watanabe | 燃料電池等のbfe型電極 |
EP0558142A1 (en) * | 1992-02-26 | 1993-09-01 | Stork Screens B.V. | Method for the production of a metal foam and a metal foam obtained |
JPH07326361A (ja) * | 1994-05-31 | 1995-12-12 | Toyota Motor Corp | 電極とその製造方法および燃料電池 |
WO1997020358A1 (de) * | 1995-11-28 | 1997-06-05 | Hoechst Research & Technology Deutschland Gmbh & Co. Kg | Gasdiffusionselektrode für polymerelektrolytmembran-brennstoffzellen |
JPH1040932A (ja) * | 1996-07-26 | 1998-02-13 | Honda Motor Co Ltd | 固体高分子電解質膜の両面に電極を配設した組立体の製造方法および装置 |
WO2002058178A1 (fr) * | 2001-01-19 | 2002-07-25 | Matsushita Electric Industrial Co., Ltd. | Procede de fabrication d'une liaison film electrolytique-electrode de pile a combustible |
JP2002280003A (ja) * | 2001-03-21 | 2002-09-27 | Matsushita Electric Ind Co Ltd | 高分子電解質型燃料電池用電極と電解質膜電極接合体の製造方法 |
-
2002
- 2002-10-21 JP JP2002306153A patent/JP4355822B2/ja not_active Expired - Fee Related
-
2003
- 2003-10-21 AU AU2003273068A patent/AU2003273068A1/en not_active Abandoned
- 2003-10-21 CA CA002503158A patent/CA2503158A1/en not_active Abandoned
- 2003-10-21 US US10/532,010 patent/US20060141336A1/en not_active Abandoned
- 2003-10-21 WO PCT/JP2003/013449 patent/WO2004036673A1/ja active Application Filing
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6229069A (ja) * | 1985-07-30 | 1987-02-07 | Masahiro Watanabe | 燃料電池等のbfe型電極 |
EP0558142A1 (en) * | 1992-02-26 | 1993-09-01 | Stork Screens B.V. | Method for the production of a metal foam and a metal foam obtained |
JPH07326361A (ja) * | 1994-05-31 | 1995-12-12 | Toyota Motor Corp | 電極とその製造方法および燃料電池 |
WO1997020358A1 (de) * | 1995-11-28 | 1997-06-05 | Hoechst Research & Technology Deutschland Gmbh & Co. Kg | Gasdiffusionselektrode für polymerelektrolytmembran-brennstoffzellen |
JPH1040932A (ja) * | 1996-07-26 | 1998-02-13 | Honda Motor Co Ltd | 固体高分子電解質膜の両面に電極を配設した組立体の製造方法および装置 |
WO2002058178A1 (fr) * | 2001-01-19 | 2002-07-25 | Matsushita Electric Industrial Co., Ltd. | Procede de fabrication d'une liaison film electrolytique-electrode de pile a combustible |
JP2002280003A (ja) * | 2001-03-21 | 2002-09-27 | Matsushita Electric Ind Co Ltd | 高分子電解質型燃料電池用電極と電解質膜電極接合体の製造方法 |
Also Published As
Publication number | Publication date |
---|---|
AU2003273068A8 (en) | 2004-05-04 |
CA2503158A1 (en) | 2004-04-29 |
AU2003273068A1 (en) | 2004-05-04 |
JP4355822B2 (ja) | 2009-11-04 |
JP2004146076A (ja) | 2004-05-20 |
US20060141336A1 (en) | 2006-06-29 |
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