WO2005043656A1 - 固体高分子電解質型燃料電池用ガス拡散層 - Google Patents
固体高分子電解質型燃料電池用ガス拡散層 Download PDFInfo
- Publication number
- WO2005043656A1 WO2005043656A1 PCT/JP2004/016163 JP2004016163W WO2005043656A1 WO 2005043656 A1 WO2005043656 A1 WO 2005043656A1 JP 2004016163 W JP2004016163 W JP 2004016163W WO 2005043656 A1 WO2005043656 A1 WO 2005043656A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- gas diffusion
- diffusion layer
- fuel cell
- polymer electrolyte
- mass
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Ceased
Links
Classifications
-
- 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
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/023—Porous and characterised by the material
- H01M8/0234—Carbonaceous material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B82—NANOTECHNOLOGY
- B82Y—SPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
- B82Y30/00—Nanotechnology for materials or surface science, e.g. nanocomposites
-
- 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
-
- 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
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/023—Porous and characterised by the material
- H01M8/0239—Organic resins; Organic polymers
-
- 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
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/023—Porous and characterised by the material
- H01M8/0241—Composites
- H01M8/0243—Composites in the form of mixtures
-
- 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
Definitions
- the present invention relates to a novel gas diffusion layer in a solid polymer electrolyte fuel cell, and a solid polymer electrolyte fuel cell provided with the gas diffusion layer.
- a general single cell of a solid polymer electrolyte fuel cell has a structure in which an anode electrode layer and a force source electrode layer are arranged with a cation exchange membrane, which is a solid polymer electrolyte, interposed therebetween.
- an anode gas diffusion layer and a force electrode gas diffusion layer for supplying hydrogen gas and oxygen gas to the electrode layer and passing and discharging the generated moisture to the outside are arranged.
- a separator having a groove for a gas flow path formed on the surface thereof is arranged to form a single cell.
- the anode electrode layer and the force electrode layer are generally formed by hot pressing a thin film formed of conductive carbon carrying a platinum catalyst and an ion exchange resin.
- the surface of the catalyst is covered with water by water or the like generated by a force reaction that requires a smooth reaction at the three-phase interface between the catalyst phase and the gas phase, and the gas phase and the electrolyte phase. Since contact with gas or hydrogen gas is hindered, it is important to remove generated water smoothly from the electrode layer.
- Patent Document 2 discloses that a composition containing conductive granules, water-repellent resin, and fibrous carbon is applied or impregnated on the surface of a conductive porous substrate such as carbon cloth. A gas diffusion layer formed by the method is described. As fibrous carbon, the use of vapor-grown carbon fiber with a fiber diameter of 500 nm or less is described, but there is still room for improvement in characteristics such as output voltage, output current, electric resistance, and mechanical strength. Have left.
- Patent Document 1 Japanese Patent Application Laid-Open No. 2001-6699
- Patent Document 2 JP 2003-115302 A
- the present invention relates to a gas diffusion layer of a solid polymer electrolyte fuel cell, which has been conventionally insufficient in characteristics and is required to be improved in characteristics. Gas and oxygen gas can be supplied smoothly, and the generated moisture can be removed smoothly to the outside.In addition, it has excellent characteristics such as current density and output voltage. It is an object of the present invention to provide a gas diffusion layer which has stable performance over a long period of time because of its high mechanical strength, and a solid polymer electrolyte fuel cell provided with the gas diffusion layer. Means for solving the problem
- the present inventor has conducted studies to achieve the above object, and found that fine carbon fibers having a specific range in which the fiber diameter / the fiber length is extremely small and the structure of which is a specific shape are obtained.
- the present inventors have found that a gas diffusion layer formed from a papermaking product from a mixture containing the fine carbon fibers in a specific ratio together with the conductive particles and the water-repellent resin particles has unexpectedly excellent properties.
- the present inventors have found that, when the above-mentioned fine carbon fiber is subjected to a specific heat treatment, a gas diffusion layer having further improved properties is obtained, and the mixture forming the gas diffusion layer contains: Along with the fine carbon fiber, the fiber diameter is smaller than that of the fine carbon fiber. It has been found that a gas diffusion layer formed by a papermaking mixture of a mixture containing medium and fine carbon fibers having a large fiber length in a specific ratio has excellent characteristics.
- the present invention is based on the new knowledge as described above, and has the following gist.
- a gas diffusion layer for a polymer electrolyte fuel cell comprising a 2 mm sheet-like molded product.
- Fine carbon fiber strength The polymer electrolyte type according to the above (1) or (2), which is heat-treated in a non-oxidizing atmosphere at a temperature of 2300 ° C. or more in the presence of a boron compound. Gas diffusion layer for fuel cells.
- the conductive particles are at least one selected from the group consisting of carbon black, furnace black, acetylene black, thermal black, channel black, and Ketjen black.
- the gas diffusion layer for a polymer electrolyte fuel cell according to the above.
- a polymer electrolyte fuel cell comprising the gas diffusion layer according to any one of (1) to (6) above.
- the gas diffusion layer for a polymer electrolyte fuel cell according to the present invention is a fine particle having extremely high conductivity and mechanical strength, which is uniformly dispersed throughout the gas diffusion layer. Due to the presence of the carbon fiber, hydrogen gas and oxygen gas can be smoothly supplied to the electrode layer, and moisture generated in the electrode layer can be smoothly removed to the outside. Furthermore, as a result of reducing the electric resistance of the gas diffusion layer, the gas diffusion layer having excellent characteristics such as output power density and output voltage, and having stable performance over a long period, and the gas diffusion layer are provided. A solid polymer electrolyte fuel cell is provided.
- the fine carbon fiber used in the present invention has a fiber diameter of 0.5 to 500 nm, a fiber length of 1000 ⁇ m or less, preferably has an aspect ratio of 3 to 1000, and preferably has a carbon hexagonal mesh surface.
- a fine carbon fiber having a multilayer structure in which cylinders are arranged concentrically and whose central axis is a hollow structure is used.
- Large fine carbon fibers are significantly different from conventional carbon fibers with a fiber diameter of 5 to 15 m, which are obtained by heat-treating conventional PAN, pitch, cellulose, rayon and other fibers.
- the fine carbon fibers used in the present invention not only differ in fiber diameter / fiber length, but also in structure, as compared with conventional carbon fibers. As a result, it is extremely excellent in physical properties such as electrical conductivity and thermal conductivity.
- the fine carbon fiber used in the present invention has a fiber diameter smaller than 0.5 nm, the obtained gas diffusion layer has insufficient mechanical strength.
- the fiber diameter is larger than 500 nm or when the fiber length is longer than 1000 m, it becomes difficult for the fine carbon fibers to be uniformly dispersed in the gas diffusion layer, and the characteristics of the gas diffusion layer deteriorate. I will.
- the fine carbon fibers used in the present invention are particularly preferably those having a fiber diameter of 10 to 200 nm, a fiber length of 3 to 300 m, and preferably an aspect ratio of 5 to 300.
- a preferred fine carbon fiber used in the present invention is a carbon nanotube.
- This carbon nanotube is also called a graphite whisker, a filamentous carbon, a carbon fiber, or the like. In the present invention, any of them can be used. However, multi-walled carbon nanotubes are preferred because they can provide high mechanical strength and are economically advantageous.
- the carbon nanotube used in the present invention is, for example, a "carbon nanotube base". It is manufactured by an arc discharge method, a laser evaporation method, a pyrolysis method, etc., as described in “Foundations” (Corona Publishing, pp. 23-57, 1998).
- the carbon nanotube has a fiber diameter of preferably 0.5-500 nm, a fiber length of preferably 1-1500 m, and preferably an aspect ratio of -500.
- VGCF Vapor-grown carbon fiber
- a gas such as a hydrocarbon is used in the presence of an organic transition metal-based catalyst. It is produced by pyrolysis under gas phase with hydrogen gas below.
- This vapor grown carbon fiber has a fiber diameter of preferably 50 to 300 nm, a fiber length of preferably 3 to 300 ⁇ m, and preferably an aspect ratio of 3 to 500. This VGCF is excellent in terms of manufacturability, handling, and properties.
- the fiber diameter ⁇ ⁇ fiber length of the fine carbon fibers can be measured by an electron microscope.
- the fine carbon fiber used in the present invention is preferably heat-treated in a non-oxidizing atmosphere at a temperature of 2300 ° C or more, preferably 2500 to 3500 ° C, so that its mechanical strength is high. Greatly improves the chemical stability and contributes to the weight reduction of the pressure vessel.
- argon, helium, or nitrogen gas is preferably used as the non-oxidizing atmosphere.
- a boron compound such as boron carbide, boron oxide, boric acid, borate, boron nitride, or an organic boron compound coexists, the heat treatment effect is further improved and the heat treatment temperature is lowered. , Can be advantageously implemented.
- This boron compound is preferably present in the heat-treated fine carbon fiber so that the boron content is 0.01 to 10% by mass, preferably 0.1 to 5% by mass.
- conductive particles used for forming the gas diffusion layer of the present invention conductive particles having an average primary particle size of preferably 1 ⁇ m or less, particularly preferably 0.5 ⁇ m or less are used. Is done.
- the average secondary particle diameter is preferably about 15 m or less.
- Preferred examples thereof include carbon particles of carbon black, furnace black, acetylene black and thermal black.
- the conductive fibers used in place of or simultaneously with the conductive particles include: The diameter and length used for so-called carbon paper, carbon cloth, etc. are preferred. Channel black and at least one carbon fiber whose Ketjen black or group power is also selected. Of these, carbon black and acetylene black are preferred as the conductive particles.
- the water-repellent resin particles used for forming the gas diffusion layer of the present invention it is preferable to use fluorine resin particles.
- the fluorine resin particles include polytetrafluoroethylene (PTFE), polyvinylidene fluoride (PVDF), and tetrafluoroethylene-hexafluoroethylene copolymer.
- the average primary particle size is preferably 1 m or less, particularly 0.5 ⁇ m or less.
- the average secondary particle diameter is preferably about 15 ⁇ m or less.
- a gas diffusion layer is formed from fine carbon fibers, conductive particles, and water-repellent resin particles, they are formed into a uniform mixture.
- the fine carbon fibers, conductive particles, and water-repellent resin particles are used.
- the mixing ratio of the aqueous resin particles is important. The mixing ratio is 5 to 50% by mass of fine carbon fibers, 35 to 90% by mass of conductive particles, and 5 to 15% by mass of water-repellent resin particles. If the amount of the fine carbon fibers is too large, the gas diffusivity decreases. Conversely, if the amount of the fine carbon fibers is too small, the strength decreases or the electric resistance increases, and the object of the present invention cannot be achieved.
- the amount of the conductive particles is too large, the gas diffusibility decreases, and if the amount of the conductive particles is too small, the electric resistance increases, and the object of the present invention cannot be achieved. If the amount of the water-repellent resin particles is too large, the gas diffusibility will be reduced, and if the amount of the water-repellent resin particles is too small, the water repellency will be insufficient, and the object of the present invention cannot be achieved.
- the mixing ratio of the fine carbon fibers, the conductive particles, and the water-repellent resin particles is 8 to 40% by mass of the fine carbon fibers and 47 to 85% by mass of the conductive particles. % And the water-repellent resin particles 7 to 13% by mass are preferable for the characteristics of the gas diffusion layer.
- the fine carbon fiber, the conductive particles, and the water-repellent resin particles are sufficiently uniformly mixed, but a mixing means such as a kneader or a grinder is used. Is mixed uniformly using a machine.
- a medium-fine carbon fiber having a fiber diameter of 0.5-500 / zm and a fiber length of 0.08-100mm together with the fine carbon fiber, the conductive particles and the water-repellent resin particles is used.
- Fiber can be used.
- Machine of gas diffusion layer obtained by using kagurumi medium and fine carbon fiber This is preferable since the target strength and gas diffusibility are improved.
- Organic carbon fibers obtained by heat-treating and carbonizing fibers such as PAN, pitch, and cellulose can be used as the medium and fine carbon fibers.
- the strong medium and fine carbon fibers can be contained in the mixture forming the gas diffusion layer preferably in an amount of 5 to 55% by mass, particularly preferably 10 to 40% by mass.
- a slurry is obtained by mixing the above-mentioned fine carbon fibers, conductive particles, water-repellent resin particles, and preferably contained medium-fine carbon fibers obtained by force using water or the like as a dispersion medium.
- the mixture is formed into a sheet and molded into a sheet.
- a papermaking method an existing method can be adopted, and a round-mesh paper machine or the like is used.
- a binder is used, if necessary, to facilitate molding. Oil pitch can be used as the binder.
- a sheet-shaped molded product having a thickness of preferably 0.05 to 2 mm, particularly preferably 0.1 to 1 mm is obtained.
- VGCF graphitized VGCF having a fiber diameter of 100 nm and a fiber length of 100 m
- 80% by mass of acetylene black having an average particle size of 30 nm was used as conductive particles.
- the gas-dispersing layer which is formed by sheeting a mixture of PTFE resin having an average secondary particle diameter of 10% by mass as the aqueous resin particles, and has a sheet-like molded product having a thickness of 0.5 mm, has the above-mentioned VGCF graphite layer.
- the polymer electrolyte fuel cell provided with the gas diffusion layer according to the present invention is excellent in characteristics such as output power density and output voltage, and further has a long mechanical strength such as bending strength. Since it has stable performance over the range, the characteristics of the polymer electrolyte fuel cell are further improved.
- the polymer electrolyte fuel cell obtained by packing can be operated at low temperature, and it has low weight and easy handling. It is a suitable power source for the body.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Electrochemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Sustainable Energy (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Manufacturing & Machinery (AREA)
- Composite Materials (AREA)
- Nanotechnology (AREA)
- Physics & Mathematics (AREA)
- Condensed Matter Physics & Semiconductors (AREA)
- General Physics & Mathematics (AREA)
- Materials Engineering (AREA)
- Crystallography & Structural Chemistry (AREA)
- Inert Electrodes (AREA)
- Fuel Cell (AREA)
Abstract
Description
Claims
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2005515189A JPWO2005043656A1 (ja) | 2003-10-30 | 2004-10-29 | 固体高分子電解質型燃料電池用ガス拡散層 |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2003-370150 | 2003-10-30 | ||
| JP2003370150 | 2003-10-30 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2005043656A1 true WO2005043656A1 (ja) | 2005-05-12 |
Family
ID=34543850
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/JP2004/016163 Ceased WO2005043656A1 (ja) | 2003-10-30 | 2004-10-29 | 固体高分子電解質型燃料電池用ガス拡散層 |
Country Status (2)
| Country | Link |
|---|---|
| JP (1) | JPWO2005043656A1 (ja) |
| WO (1) | WO2005043656A1 (ja) |
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2005285370A (ja) * | 2004-03-26 | 2005-10-13 | Japan Vilene Co Ltd | ガス拡散電極前駆体、ガス拡散電極、燃料電池、及びガス拡散電極前駆体の製造方法 |
| JP2007141783A (ja) * | 2005-11-22 | 2007-06-07 | Nitto Denko Corp | 燃料電池用ガス拡散層とその製造方法ならびにそれを用いた燃料電池 |
| JP2009211869A (ja) * | 2008-03-03 | 2009-09-17 | Dainippon Printing Co Ltd | 固体高分子形燃料電池用触媒層及びその製造方法 |
| JP2010015908A (ja) * | 2008-07-04 | 2010-01-21 | Noritake Co Ltd | ガス拡散電極用基材、その製造方法、および膜−電極接合体 |
| JP2011054449A (ja) * | 2009-09-02 | 2011-03-17 | Noritake Co Ltd | ガス拡散電極用基材、その製造方法、および膜−電極接合体 |
| CN102203995A (zh) * | 2008-10-31 | 2011-09-28 | 松下电器产业株式会社 | 燃料电池用气体扩散层及其制造方法、膜电极接合体以及燃料电池 |
| JP2011198520A (ja) * | 2010-03-17 | 2011-10-06 | Nihon Gore Kk | 固体高分子形燃料電池ガス拡散層 |
| EP2343762A4 (en) * | 2008-10-31 | 2012-05-09 | Panasonic Corp | MEMBRANE ELECTRODE ASSEMBLY AND FUEL CELL |
| JP2015032470A (ja) * | 2013-08-02 | 2015-02-16 | 日本バイリーン株式会社 | ガス拡散電極用基材、ガス拡散電極、膜−電極接合体及び固体高分子形燃料電池 |
| WO2015098089A1 (ja) * | 2013-12-27 | 2015-07-02 | 日本ゼオン株式会社 | 導電膜、燃料電池用ガス拡散層、燃料電池用触媒層、燃料電池用電極、燃料電池用膜電極接合体、及び燃料電池 |
| US9525187B2 (en) | 2012-02-08 | 2016-12-20 | Toyota Jidosha Kabushiki Kaisha | Gas diffusion layer for fuel cell, fuel cell, and method of manufacturing gas diffusion layer for fuel cell |
| EP3579315A1 (en) | 2018-06-07 | 2019-12-11 | Panasonic Intellectual Property Management Co., Ltd. | Gas diffusion layer for fuel battery, membrane electrode assembly, and fuel battery |
| JP2019216084A (ja) * | 2018-06-07 | 2019-12-19 | パナソニックIpマネジメント株式会社 | 燃料電池用ガス拡散層、膜電極接合体、及び燃料電池 |
| CN116387532A (zh) * | 2023-03-24 | 2023-07-04 | 中国科学技术大学 | 氢气电极及其制备方法和应用 |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS56102081A (en) * | 1980-01-19 | 1981-08-15 | Sanyo Electric Co Ltd | Manufacture of gas-diffusion electrode |
| JP2001283878A (ja) * | 2000-03-30 | 2001-10-12 | Toray Ind Inc | 導電シートおよび該シートを用いた燃料電池用電極 |
| JP2003115302A (ja) * | 2001-01-16 | 2003-04-18 | Showa Denko Kk | 電池用触媒組成物、ガス拡散層及びこれらを備えた燃料電池 |
-
2004
- 2004-10-29 JP JP2005515189A patent/JPWO2005043656A1/ja active Pending
- 2004-10-29 WO PCT/JP2004/016163 patent/WO2005043656A1/ja not_active Ceased
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS56102081A (en) * | 1980-01-19 | 1981-08-15 | Sanyo Electric Co Ltd | Manufacture of gas-diffusion electrode |
| JP2001283878A (ja) * | 2000-03-30 | 2001-10-12 | Toray Ind Inc | 導電シートおよび該シートを用いた燃料電池用電極 |
| JP2003115302A (ja) * | 2001-01-16 | 2003-04-18 | Showa Denko Kk | 電池用触媒組成物、ガス拡散層及びこれらを備えた燃料電池 |
Cited By (21)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2005285370A (ja) * | 2004-03-26 | 2005-10-13 | Japan Vilene Co Ltd | ガス拡散電極前駆体、ガス拡散電極、燃料電池、及びガス拡散電極前駆体の製造方法 |
| JP2007141783A (ja) * | 2005-11-22 | 2007-06-07 | Nitto Denko Corp | 燃料電池用ガス拡散層とその製造方法ならびにそれを用いた燃料電池 |
| JP2009211869A (ja) * | 2008-03-03 | 2009-09-17 | Dainippon Printing Co Ltd | 固体高分子形燃料電池用触媒層及びその製造方法 |
| JP2010015908A (ja) * | 2008-07-04 | 2010-01-21 | Noritake Co Ltd | ガス拡散電極用基材、その製造方法、および膜−電極接合体 |
| CN102203995B (zh) * | 2008-10-31 | 2015-01-21 | 松下电器产业株式会社 | 燃料电池用气体扩散层及其制造方法、膜电极接合体以及燃料电池 |
| JP2011210737A (ja) * | 2008-10-31 | 2011-10-20 | Panasonic Corp | 燃料電池用ガス拡散層及びその製造方法、膜電極接合体、並びに燃料電池 |
| EP2348564A4 (en) * | 2008-10-31 | 2012-05-09 | Panasonic Corp | GAS DISPERSION LAYER FOR A FUEL CELL, MANUFACTURING METHOD, AND MEMBRANE ELECTRODE ASSEMBLY AND FUEL CELL |
| EP2343762A4 (en) * | 2008-10-31 | 2012-05-09 | Panasonic Corp | MEMBRANE ELECTRODE ASSEMBLY AND FUEL CELL |
| US8999603B2 (en) | 2008-10-31 | 2015-04-07 | Panasonic Corporation | Gas diffusion layer for fuel cell, manufacturing method therefor, membrane electrode assembly, and fuel cell |
| CN102203995A (zh) * | 2008-10-31 | 2011-09-28 | 松下电器产业株式会社 | 燃料电池用气体扩散层及其制造方法、膜电极接合体以及燃料电池 |
| JP2011054449A (ja) * | 2009-09-02 | 2011-03-17 | Noritake Co Ltd | ガス拡散電極用基材、その製造方法、および膜−電極接合体 |
| JP2011198520A (ja) * | 2010-03-17 | 2011-10-06 | Nihon Gore Kk | 固体高分子形燃料電池ガス拡散層 |
| US9525187B2 (en) | 2012-02-08 | 2016-12-20 | Toyota Jidosha Kabushiki Kaisha | Gas diffusion layer for fuel cell, fuel cell, and method of manufacturing gas diffusion layer for fuel cell |
| JP2015032470A (ja) * | 2013-08-02 | 2015-02-16 | 日本バイリーン株式会社 | ガス拡散電極用基材、ガス拡散電極、膜−電極接合体及び固体高分子形燃料電池 |
| WO2015098089A1 (ja) * | 2013-12-27 | 2015-07-02 | 日本ゼオン株式会社 | 導電膜、燃料電池用ガス拡散層、燃料電池用触媒層、燃料電池用電極、燃料電池用膜電極接合体、及び燃料電池 |
| JPWO2015098089A1 (ja) * | 2013-12-27 | 2017-03-23 | 日本ゼオン株式会社 | 導電膜、燃料電池用ガス拡散層、燃料電池用触媒層、燃料電池用電極、燃料電池用膜電極接合体、及び燃料電池 |
| EP3579315A1 (en) | 2018-06-07 | 2019-12-11 | Panasonic Intellectual Property Management Co., Ltd. | Gas diffusion layer for fuel battery, membrane electrode assembly, and fuel battery |
| JP2019216084A (ja) * | 2018-06-07 | 2019-12-19 | パナソニックIpマネジメント株式会社 | 燃料電池用ガス拡散層、膜電極接合体、及び燃料電池 |
| US10978716B2 (en) | 2018-06-07 | 2021-04-13 | Panasonic Intellectual Property Management Co., Ltd. | Gas diffusion layer for fuel battery, membrane electrode assembly, and fuel battery |
| JP7249574B2 (ja) | 2018-06-07 | 2023-03-31 | パナソニックIpマネジメント株式会社 | 燃料電池用ガス拡散層、膜電極接合体、及び燃料電池 |
| CN116387532A (zh) * | 2023-03-24 | 2023-07-04 | 中国科学技术大学 | 氢气电极及其制备方法和应用 |
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| JPWO2005043656A1 (ja) | 2007-11-29 |
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