WO2007043587A1 - 膜電極接合体および固体高分子形燃料電池 - Google Patents
膜電極接合体および固体高分子形燃料電池 Download PDFInfo
- Publication number
- WO2007043587A1 WO2007043587A1 PCT/JP2006/320337 JP2006320337W WO2007043587A1 WO 2007043587 A1 WO2007043587 A1 WO 2007043587A1 JP 2006320337 W JP2006320337 W JP 2006320337W WO 2007043587 A1 WO2007043587 A1 WO 2007043587A1
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- WIPO (PCT)
- Prior art keywords
- polymer electrolyte
- electrolyte membrane
- membrane
- layer
- electrode layer
- Prior art date
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- 238000000034 method Methods 0.000 description 9
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- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
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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
- 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
-
- 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
-
- 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
- H01M8/0271—Sealing or supporting means around electrodes, matrices or membranes
- H01M8/0273—Sealing or supporting means around electrodes, matrices or membranes with sealing or supporting means in the form of a frame
-
- 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
- H01M8/0271—Sealing or supporting means around electrodes, matrices or membranes
- H01M8/0276—Sealing means characterised by their form
-
- 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
-
- 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
- H01M8/0271—Sealing or supporting means around electrodes, matrices or membranes
- H01M8/028—Sealing means characterised by their material
-
- 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
- H01M8/0271—Sealing or supporting means around electrodes, matrices or membranes
- H01M8/0286—Processes for forming seals
-
- 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
- H01M8/0297—Arrangements for joining electrodes, reservoir layers, heat exchange units or bipolar separators to each other
-
- 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
- H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
- H01M8/241—Grouping of fuel cells, e.g. stacking of fuel cells with solid or matrix-supported electrolytes
- H01M8/242—Grouping of fuel cells, e.g. stacking of fuel cells with solid or matrix-supported electrolytes comprising framed electrodes or intermediary frame-like gaskets
-
- 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 membrane electrode assembly constituting a solid polymer fuel cell and a solid polymer fuel cell using the same.
- a fuel cell generates electricity and heat simultaneously by electrochemically reacting a fuel gas mainly composed of hydrogen and an oxidant gas such as air, and does not generate carbon dioxide. It is attracting attention as a power generation system, and various types have been developed. Among them, fuel cells using polymer electrolyte membranes (hereinafter referred to as “solid polymer fuel cells”) are superior to other fuel cells in terms of start-up performance and provide high output density. Miniaturization is possible. Therefore, it is expected to be widely applied as a power source for electric vehicles and homes.
- This polymer electrolyte fuel cell includes a polymer electrolyte membrane that selectively permeates protons and a pair of catalyst electrodes formed on both sides of the polymer electrolyte membrane as one of the constituent elements.
- the catalyst electrode is mainly composed of carbon powder supporting a platinum-based metal catalyst, and is formed on both surfaces of the polymer electrolyte membrane and on the outer surface of the catalyst layer. It consists of a gas diffusion layer that has both gas and electronic conductivity.
- the unit in which the polymer electrolyte membrane and the catalytic electrode force are also composed is called a membrane electrode assembly.
- a gas seal member and a gasket are arranged around the electrode with a polymer electrolyte membrane interposed so that the supplied fuel gas and oxidant gas do not leak outside the cell or mix with each other. Is done.
- a conductive separator plate for mechanically fixing them and electrically connecting adjacent membrane electrode assemblies to each other in series is arranged.
- This separator plate has a gas flow path for supplying reaction gas to the electrode surface and carrying away generated gas and surplus gas.
- the gas flow path can be provided separately from the separator plate.
- a gas flow path is formed by providing a groove on the surface of the force separator plate.
- a gasket of a polymer electrolyte fuel cell is used to make contact between a separator plate and an electrode.
- a gasket In order to perform a gas seal, it is necessary to have high dimensional accuracy, sufficient elasticity, and sufficient interference. For this reason, a sheet-like gasket that has a strength such as rubber,
- o-rings with rubber strength are used.
- Japanese Patent Application Laid-Open No. 2004-303723 discloses a polymer fuel cell in which a gas seal member is in contact with an electrolyte membrane portion protruding from the electrode portion in a frame shape.
- the air electrode side of the gas seal member is in contact with the electrolyte membrane in a planar shape, while the fuel electrode side is a rib and is in linear contact.
- This gas seal member is composed of a resin film such as polyimide, a pressure-sensitive adhesive layer, and a rubber layer, and has a large number of parts. Therefore, it is difficult to assemble, and displacement between parts is likely to occur, and there is a risk of gas leakage due to poor assembly. Further, since one of the gas seal members disclosed in Japanese Patent Laid-Open No. 2004-303723 is a rib, a local force is applied to the electrolyte membrane when a pressure of 4 is applied to reduce gas leakage. In recent years, thin film electrolyte membranes have been attempted to further improve power generation efficiency, but there is a risk of damage to the electrolyte membrane when local force is applied to the thin electrolyte membrane.
- a membrane electrode assembly for a polymer fuel cell which is intended to be surely set by reducing the number of parts, is described in JP-A-8-45517.
- This technique can increase the mechanical strength even when a thin electrolyte membrane is used.
- a five-layer structure composed of an electrolyte membrane, two electrodes, and two diffusion layers is sandwiched and integrated with a seal member having a hard polymer force such as a rubber-like elastic body or polyimide.
- Japanese Patent Laid-Open No. 6-333582 discloses a gas seal member, an electrode, and a solid polymer fuel cell in order to prevent deformation (creep) due to continuous gas pressure on the electrolyte membrane.
- a technique for providing a spacer made of a special metal, a thermosetting resin or a heat-resistant thermoplastic resin is disclosed. The spacer thickness is set to be thinner than the thickness of each electrode, and the electrolyte membrane is protected from the pressure applied to the electrolyte membrane through the electrodes.
- a member for gas-sealing the electrolyte membrane of a polymer electrolyte fuel cell that has been thinned in recent years a member in contact with the electrolyte membrane in a planar shape is preferable from the viewpoint of improving the strength. That is, such a gas seal member also has an action as a reinforcing member for the electrolyte membrane.
- a material such as rubber having a large elongation is inferior in terms of reinforcement of the electrolyte membrane and adhesion with the electrolyte membrane.
- thermosetting resin having higher strength is preferable.
- thermosetting resin film is thermocompression bonded to an electrolyte membrane used in a polymer electrolyte fuel cell, the polymer electrolyte membrane is altered. It was.
- the problems to be solved by the present invention include a member that is excellent in gas sealability and can improve the strength of the electrolyte membrane, is not accompanied by alteration of the polymer electrolyte membrane, and has a small number of components.
- An object of the present invention is to provide a membrane electrode assembly that can be easily assembled and a polymer electrolyte fuel cell using the membrane electrode assembly.
- the present inventors have advanced research on the cause of electrolyte membrane alteration when gas-sealing and reinforcing the electrolyte membrane of a solid polymer fuel cell with a thermosetting resin sheet to solve the above problems. It was. As a result, such alteration is caused by the heat generated by thermocompression bonding of the B-stage thermosetting resin sheet to the electrolyte membrane and further thermosetting, and the thermosetting resin components such as the main agent and curing agent. I found out that it is the cause.
- the gas sealing property can be further improved and the deterioration of the electrolyte membrane can be suppressed.
- the present invention was completed by finding out what can be done.
- a membrane electrode assembly for a polymer electrolyte fuel cell according to the present invention comprises:
- the plane area of the polymer electrolyte membrane is slightly larger than the plane area of the fuel electrode layer and the air electrode layer.
- a protective layer is present at least partially between the polymer electrolyte membrane and the reinforcing frame.
- a fiber reinforced frame is preferable. Since such a reinforcing frame has high strength, the strength of the membrane electrode assembly can be increased as a result, and the handling thereof becomes easy.
- thermosetting resin constituting the reinforcing frame penetrates into and cures at least part of the outer periphery of the fuel electrode diffusion layer and the Z or air electrode diffusion layer. Is preferred. This is because such a membrane electrode assembly is extremely excellent in gas sealability.
- the membrane electrode assembly it is preferable that at least the outer side of the flat part of the reinforcing frame, that is, the flat part on the side in contact with the gasket is smoothened. This is because such a membrane electrode assembly is excellent in adhesion to the gasket.
- a polymer electrolyte fuel cell of the present invention has the membrane electrode assembly.
- the membrane / electrode assembly of the present invention is easy to handle because the strength is enhanced by the reinforcing frame even when a thin polymer electrolyte membrane having excellent power generation efficiency but poor strength is used. It is. In addition, alteration of the polymer electrolyte membrane caused by thermosetting resin, which is a problem in conventional membrane electrode assemblies, can be suppressed by the protective layer. In addition, since the number of parts is small, assembly is easy and the possibility of assembly failure is low. Therefore, the present invention is extremely useful industrially as a polymer electrolyte fuel cell expected to be put to practical use in the future.
- FIG. 1 is a view schematically showing a cross section of a membrane electrode assembly of the present invention.
- 1 indicates a polymer electrolyte membrane
- 2 indicates an electrode layer
- 3 indicates a gas diffusion layer
- 4 indicates a protective layer
- 5 indicates a reinforcing frame.
- a membrane electrode assembly for a polymer electrolyte fuel cell according to the present invention comprises:
- the plane area of the polymer electrolyte membrane is slightly larger than the plane area of the fuel electrode layer and air electrode layer, and forms a fuel electrode layer or air electrode layer on one or both sides of the polymer electrolyte membrane.
- Reinforcement frame made of thermosetting resin is placed on
- a protective layer is present at least partially between the polymer electrolyte membrane and the reinforcing frame.
- the polymer electrolyte membrane used in the present invention may be one generally used in solid polymer fuel cells.
- a perfluorinated electrolyte or a hydrocarbon based electrolyte can be suitably used, and a perfluorinated electrolyte membrane is particularly preferable.
- sulfonic acid electrolyte membranes such as naphthion (registered trademark) manufactured by DuPont and GORE-S ELECT (registered trademark) manufactured by Japan Gore-Tex can be used.
- a perfluorosulfonic acid resin membrane reinforced with stretched porous polytetrafluoroethylene such as GORE-SELECT (registered trademark) manufactured by Japan Goatex is suitable.
- GORE-SELECT registered trademark
- it is reinforced with expanded porous polytetrafluoroethylene it is excellent in strength.
- the thickness of the polymer electrolyte membrane is generally about 10 to 30 m in consideration of power generation efficiency and strength.
- the catalyst electrode layer those generally used in polymer electrolyte fuel cells can be used.
- conductive carbon fine particles such as bonbon black with fine particles of platinum or an alloy of platinum and other metal supported on the surface, and polymer solutions such as perfluorosulfonic acid resin solution are suitable.
- metals that can be alloyed with platinum include Ru, Rh, Mo, Cr, Co, and Fe.
- the average particle size of the gold-enriched fine particles as the catalyst component is preferably about lOnm or less.
- the average particle size of the conductive carbon fine particles is preferably about 20: LOOnm. Ethanol or the like can be used as a solvent for the ink.
- the amount of platinum in the fuel electrode layer is 0.5 in terms of metallic platinum 03-0. 5mgZcm 2 about the desirable
- the amount of platinum in the air electrode layer is preferably about 0.1 to 0.8 mgZcm 2 in terms of metallic platinum.
- the thickness of the fuel electrode layer and the air electrode layer (hereinafter sometimes referred to as the “electrode layer”) is
- it can be about 3 to 30 / ⁇ ⁇ .
- a fuel electrode diffusion layer and an air electrode diffusion layer (hereinafter, these may be collectively referred to as "gas diffusion layer”), respectively.
- These gas diffusion layers have a role of diffusing fuel gas or oxidant gas in the electrode layer and discharging generated water to the separator flow path.
- the material of the gas diffusion layer needs to have at least gas permeability and conductivity.
- a woven fabric made of a carbon material; a nonwoven fabric such as felt obtained by entanglement of carbon fibers; and papers such as carbon paper are widely used.
- the thickness of the gas diffusion layer is not particularly limited, but is set to 100 to 500 m, for example, because it is necessary to sufficiently diffuse the gas.
- the gas diffusion layer may be subjected to a water repellent treatment with fluorine resin or the like as necessary.
- the planar area of the polymer electrolyte membrane needs to be slightly larger than the planar areas of the fuel electrode layer and the air electrode layer.
- the strength is enhanced by reinforcing the outer periphery of the polymer electrolyte membrane without forming electrode layers on both surfaces of the polymer electrolyte membrane.
- the area on the polymer electrolyte membrane side in the plane portion of the gas diffusion layer needs to be slightly smaller than the area of the plane portion of the polymer electrolyte membrane. That is, the area of the planar portion of the polymer electrolyte membrane must be slightly larger than the surface area of the gas diffusion layer on the polymer electrolyte membrane side! / ⁇ .
- the plane area of the polymer electrolyte membrane is slightly larger than the plane area of the fuel electrode layer and the air electrode layer.
- the plane area of the electrode layer is the plane of the polymer electrolyte membrane. This means that the electrode layer is disposed on each surface of the polymer electrolyte membrane so that the electrode layer is smaller than the partial area and the outer periphery of the electrode layer does not contact the outer periphery of the polymer electrolyte membrane. This definition is the same for the surface of the gas diffusion layer on the polymer electrolyte membrane side.
- a fuel electrode layer or an air electrode layer is formed on one or both sides of the polymer electrolyte membrane, and a reinforcing frame made of a thermosetting resin is disposed on the portion. ing.
- This reinforcing frame has a role to reinforce the polymer electrolyte membrane and also serves as a fuel gas. It also has a gas sealing function to prevent leakage of oxidant gas and oxidant gas to the outside. Therefore, the reinforcing frame needs to be in a state of being in close contact with at least the peripheral surface of the gas diffusion layer.
- the thermosetting plate constituting the reinforcing frame is formed on the outer periphery of the gas diffusion layer having a porous structure. It has a structure in which fat has entered and hardened. This structure exhibits a better gas sealing property.
- thermosetting resin constituting the reinforcing frame of the present invention is not particularly limited, and examples thereof include epoxy resin, melamine resin, phenol resin, and unsaturated polyester resin. Further, a fiber reinforced frame is preferable as the reinforcing frame. The strength is higher. As the fiber that can be used here, a woven or non-woven fabric of organic fiber or glass fiber can be used. The thickness of the reinforcing frame should be determined in consideration of the thickness of the electrode layer, diffusion layer, and protective layer described later.
- the reinforcing frame may be a gas diffusion layer in which a thermosetting resin is infiltrated and cured.
- the electrode layer 2 is usually formed by making the plane area of the gas diffusion layer 3 together with the electrode layer 2 slightly smaller than the plane area of the polymer electrolyte membrane 1. Place the reinforcement frame 5 on the unexposed part (see Fig. 1 (A)). However, as shown in FIG. 1 (B), the polymer electrolyte membrane 1 and the gas diffusion layer 3 are laminated with the same plane area, and at least the polymer electrolyte membrane side surface side of the outer periphery of the gas diffusion layer 3 is laminated. It is also possible to intrude and harden the thermosetting resin and use the portion 5 ′ as a reinforcing frame.
- the polymer electrolyte membrane 1 and the gas diffusion layer 3 are laminated with the same planar area, and the reinforcing frame 5 is provided outside the laminate, at least the polymer electrolyte in the outer peripheral portion of the gas diffusion layer is provided.
- Thermosetting resin may be penetrated and cured on the film side surface (see Fig. 1 (C)).
- the part 5 ′ of the gas diffusion layer where the thermosetting resin has been infiltrated and cured is also part of the reinforcing frame.
- At least the outer side of the flat portion of the reinforcing frame is subjected to a smooth wrinkle treatment.
- the surface of the fiber reinforced thermosetting resin sheet is not necessarily smooth. Therefore, when assembling the fuel cell, it is difficult to make it closely contact with the gasket. Therefore, by performing such a smoothing treatment, the adhesion between the reinforcing frame and the gasket can be enhanced.
- a protective layer is present at least partially between the polymer electrolyte membrane and the reinforcing frame.
- This protective layer has a role of preventing contact between the polymer electrolyte membrane and the reinforcing frame, and the thermosetting resin is cured at a high temperature for curing the thermosetting resin constituting the reinforcing frame. It has the effect of suppressing the deterioration of the polymer electrolyte membrane caused by the main component and curing agent component.
- a reinforcing frame that has been heat-cured in advance is used.
- the protective layer can exert an effect of reducing damage that the dents on the surface of the reinforcing frame can damage the polymer electrolyte membrane by directly contacting the reinforcing frame and the polymer electrolyte membrane.
- the protective layer has an action of reducing damage to the reinforcing frame by preventing contact between the polymer electrolyte membrane exhibiting strong acidity and the reinforcing frame.
- “Protection” has two meanings: protection of the polymer electrolyte membrane and protection of the reinforcing frame.
- the protective layer has the effect of enhancing the adhesion between the reinforcing frame and the electrolyte membrane and enhancing the gas sealing property.
- the durability of the fuel cell is improved by forming a protective layer with a material that is highly resistant to high temperatures of about 70 to 100% RH, which is the operating atmosphere of the battery, from 70 to: It becomes possible.
- the protective layer needs to exist in a frame shape so as to surround the electrode layer and the diffusion layer at the exposed portion of the electrolyte membrane so that the reinforcing frame and the polymer electrolyte membrane do not contact each other.
- a protective layer is disposed in all parts between the reinforcing frame and the polymer electrolyte membrane.
- the resin constituting the protective layer is not particularly limited as long as it has excellent hot water resistance and acid resistance at a high temperature of 120 to 200 ° C, for example.
- polyesters such as polyethylene terephthalate; polyolefins such as polypropylene; fluorine resins such as polytetrafluoroethylene, perfluoroalkoxy fluorine resin and polyvinylidene fluoride; polyethersulfone; polyetheretherketone; Thermoplastic resins such as polysulfone can be used.
- the protective layer only needs to have a thickness sufficient to prevent the reaction between the reinforcing frame and the electrolyte membrane.
- the protective layer can have a thickness of 5 to 50 ⁇ m, and more preferably 20 ⁇ m or less.
- a fuel electrode layer and an air electrode layer are formed on both surfaces of the polymer electrolyte membrane 1.
- a high molecular weight solution for a polymer electrolyte membrane such as a perfluorosulfonic acid resin solution or a polytetrafluoroethylene dispersion is mixed.
- Carbons carrying a precious metal catalyst such as Ru are used for contact with precious metals such as Pt for the air electrode layer.
- a slurry to which carbon carrying a medium is added is prepared. This slurry is applied to the polymer electrolyte membrane by a coating method, a spray method, a transfer method, etc., and then dried to form a three-layer body. At this time, the electrode to be formed needs to be slightly smaller than the polymer electrolyte membrane.
- the fuel electrode layer or the air electrode layer is formed, and the protective layer 4 is formed on the!
- the reinforcing frame is formed on both sides, it is necessary to form the protective layer on both sides.
- the protective layer may be formed only on one side.
- a specific method for forming the protective layer is not particularly limited.
- the thermoplastic resin film described above may be formed in accordance with the shape of the exposed portion of the electrolyte membrane and may be pressure-bonded or thermocompression bonded.
- Alternatively, after coating the exposed portion of the electrolyte membrane with a melt or solution of thermoplastic resin it can be cooled and cured or dried.
- the protective layer may be formed on a three-layer body having a polymer electrolyte membrane and an electrode layer force as described above, the five-layer electrolyte membrane exposed portion in which a gas diffusion layer is further formed. It may be formed on top.
- a fuel electrode diffusion layer and an air electrode diffusion layer are formed on a three-layer body comprising a polymer electrolyte membrane 1 and an electrode layer 2 or a protective layer formed thereon. 5 layers. Specifically, for example, a cloth or paper having a porous carbon force may be bonded with an adhesive or thermocompression bonded.
- the gas diffusion layer is formed after the electrode layer is formed in the above production method, the electrode layer and the gas diffusion layer are integrated in advance by thermocompression bonding or the like, and this is combined with the polymer electrolyte. It may be attached to the film or thermocompression bonded.
- a reinforcing frame 5 made of a thermosetting resin is provided on the obtained five-layer protective layer 4, that is, on the exposed portion of the polymer electrolyte membrane.
- the method is not particularly limited, but a thermosetting resin sheet formed into a frame shape in accordance with the shape of the exposed portion of the polymer electrolyte membrane may be adhered onto the protective layer, or the polymer may be adhered to the protective layer.
- the thermoplastic resin may be coated on the protective layer and then dried.
- a B-stage epoxy sheet is laminated on the protective layer, that is, on the exposed portion of the polymer electrolyte membrane, and then placed in a mold and heat-cured to remove the mold, followed by die cutting.
- Possible methods include a fixed size, a method in which a five-layer body is set in a mold, a liquid epoxy resin is injected and cured by heating, the mold is removed, and then a predetermined size is obtained by die cutting.
- the fuel electrode diffusion layer or the air electrode diffusion layer and the reinforcing frame are integrated in advance, they are thermocompression bonded to the electrode layer 2 and the polymer electrolyte membrane 1 provided with the protective layer 4 on the outer periphery thereof. Accordingly, the target membrane electrode assembly can be obtained.
- the membrane / electrode assembly of the present invention constitutes a cell stack together with a gasket or separator and can be used as a solid polymer fuel cell.
- the membrane / electrode assembly of the present invention produced by the above method or the like, the exposed portion of the polymer electrolyte membrane, that is, the portion where the fuel electrode layer and the air electrode layer are not formed is protected with excellent adhesion. Since it is covered with a layer and a reinforcing frame that excels in strength, it excels in strength and gas sealability. Moreover, since the number of parts is small, assembly is easy. This occurs in the conventional membrane / electrode assembly in which the polymer electrolyte and the gas seal member or reinforcing member made of thermosetting resin are in direct contact with each other! This cannot occur with the membrane electrode assembly of the invention. Therefore, the membrane / electrode assembly of the present invention has a very high utility value as a constituent element of a high-quality solid polymer fuel cell.
- a 25 ⁇ m thick polyethylene naphthalate film is pressure-bonded to the exposed part of the electrolyte membrane around the electrode layer on both sides of a commercially available membrane electrode assembly (manufactured by Japan Gore-Tex, PRIMEA5510). did.
- the size of the electrolyte membrane is 80 x 80 mm, and 50 x 50 mm electrode layers are provided on both sides of the center.
- a 52 x 52mm diffusion layer (Carbel-CNWIOA, manufactured by Japan Gore-Tex) was thermocompression bonded onto the electrode layer.
- a commercially available B-stage glass epoxy sheet (manufactured by Mitsubishi Gas Chemical Company, GEPL-170) was processed into a size of 100 X 100 mm, and an opening of 52 X 52 mm was formed at the center using a blade mold. Provided.
- the obtained membrane / electrode assembly was punched into a size of 80 x 80 mm using a blade die.
- the electrolyte membrane, protective layer, and reinforcing frame were observed, but no discoloration due to alteration of the components was observed.
- a membrane / electrode assembly was obtained in the same manner as in Example 1 except that a polyethylene naphthalate film as a protective layer was not used.
- the polymer electrolyte membrane turned brown. This is thought to be due to the fact that the electrolyte membrane and the epoxy resin sheet were in direct contact with each other in the comparative example, and the reaction occurred between the two because it was held at a high temperature of 160 ° C, and the electrolyte membrane was altered. .
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Fuel Cell (AREA)
Abstract
Description
Claims
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA2624684A CA2624684C (en) | 2005-10-14 | 2006-10-11 | A membrane electrode assembly and a solid polymer electrolyte fuel cell |
DE602006018990T DE602006018990D1 (de) | 2005-10-14 | 2006-10-11 | Membranelektrolyt und verbindungsprodukt und festpolymer-elektrolyt-brennstoffbatterie |
KR1020087008770A KR101345826B1 (ko) | 2005-10-14 | 2006-10-11 | 막전극 접합체 및 고체 고분자형 연료 전지 |
EP06821834A EP1956669B1 (en) | 2005-10-14 | 2006-10-11 | Membrane electrode joint product and solid polymer electrolyte fuel battery |
US12/067,877 US20110045380A1 (en) | 2005-10-14 | 2006-11-11 | Membrane Electrode Joint Product and Solid Polymer Electrolyte Fuel Battery |
HK08109624.7A HK1116929A1 (en) | 2005-10-14 | 2008-08-29 | Membrane electrode joint product and solid polymer electrolyte fuel battery |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2005300733A JP2007109576A (ja) | 2005-10-14 | 2005-10-14 | 膜電極接合体および固体高分子形燃料電池 |
JP2005-300733 | 2005-10-14 |
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WO2007043587A1 true WO2007043587A1 (ja) | 2007-04-19 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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PCT/JP2006/320337 WO2007043587A1 (ja) | 2005-10-14 | 2006-10-11 | 膜電極接合体および固体高分子形燃料電池 |
Country Status (9)
Country | Link |
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US (1) | US20110045380A1 (ja) |
EP (1) | EP1956669B1 (ja) |
JP (1) | JP2007109576A (ja) |
KR (1) | KR101345826B1 (ja) |
CN (1) | CN101288196A (ja) |
CA (1) | CA2624684C (ja) |
DE (1) | DE602006018990D1 (ja) |
HK (1) | HK1116929A1 (ja) |
WO (1) | WO2007043587A1 (ja) |
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WO2008126350A1 (ja) * | 2007-03-14 | 2008-10-23 | Panasonic Corporation | 膜-膜補強部材接合体、膜-触媒層接合体、膜-電極接合体、高分子電解質形燃料電池、及び膜-電極接合体の製造方法 |
WO2009110154A1 (ja) * | 2008-03-07 | 2009-09-11 | ダイハツ工業株式会社 | 膜・電極接合体 |
JP2010080437A (ja) * | 2008-08-27 | 2010-04-08 | Dainippon Printing Co Ltd | 補強シート付き電解質膜−触媒層積層体及びそれを具備する固体高分子形燃料電池 |
US8524414B2 (en) | 2008-01-10 | 2013-09-03 | GM Global Technology Operations LLC | Membrane with optimized dimensions for a fuel cell |
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KR101098731B1 (ko) | 2007-05-17 | 2011-12-23 | 주식회사 엘지화학 | 연료전지용 전해질막의 보호방법, 연료전지용 막-전극접합체 및 연료전지 |
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CN103165904B (zh) * | 2011-12-19 | 2015-05-20 | 中国科学院大连化学物理研究所 | 一体式可再生燃料电池膜电极组合件及其制备方法 |
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US10326150B2 (en) * | 2014-08-26 | 2019-06-18 | Panasonic Intellectual Property Management Co., Ltd. | Fuel cell module, fuel cell stack, and method for producing fuel cell module |
JP5880669B2 (ja) * | 2014-11-20 | 2016-03-09 | 大日本印刷株式会社 | 補強シート付き電解質膜−触媒層接合体 |
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CN112447987B (zh) * | 2020-11-27 | 2022-06-28 | 上海交通大学 | 一种可满足不同增强需求的一体式膜电极制备方法 |
CN112259757B (zh) * | 2020-12-17 | 2022-05-17 | 安徽明天氢能科技股份有限公司 | 一种膜电极密封填充剂及其制备方法 |
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- 2006-10-11 WO PCT/JP2006/320337 patent/WO2007043587A1/ja active Application Filing
- 2006-10-11 EP EP06821834A patent/EP1956669B1/en not_active Not-in-force
- 2006-10-11 KR KR1020087008770A patent/KR101345826B1/ko not_active IP Right Cessation
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2008126350A1 (ja) * | 2007-03-14 | 2008-10-23 | Panasonic Corporation | 膜-膜補強部材接合体、膜-触媒層接合体、膜-電極接合体、高分子電解質形燃料電池、及び膜-電極接合体の製造方法 |
US8192896B2 (en) | 2007-03-14 | 2012-06-05 | Panasonic Corporation | Membrane-membrane reinforcing member assembly, membrane-catalyst layer assembly, membrane-electrode assembly, polymer electrolyte fuel cell, and method for manufacturing membrane-electrode assembly |
US8524414B2 (en) | 2008-01-10 | 2013-09-03 | GM Global Technology Operations LLC | Membrane with optimized dimensions for a fuel cell |
US8846265B2 (en) | 2008-01-10 | 2014-09-30 | GM Global Technology Operations LLC | Membrane with optimized dimensions for a fuel cell |
WO2009110154A1 (ja) * | 2008-03-07 | 2009-09-11 | ダイハツ工業株式会社 | 膜・電極接合体 |
JP2009217999A (ja) * | 2008-03-07 | 2009-09-24 | Daihatsu Motor Co Ltd | 膜・電極接合体 |
JP2010080437A (ja) * | 2008-08-27 | 2010-04-08 | Dainippon Printing Co Ltd | 補強シート付き電解質膜−触媒層積層体及びそれを具備する固体高分子形燃料電池 |
Also Published As
Publication number | Publication date |
---|---|
EP1956669A1 (en) | 2008-08-13 |
DE602006018990D1 (de) | 2011-01-27 |
US20110045380A1 (en) | 2011-02-24 |
CA2624684A1 (en) | 2007-04-19 |
EP1956669A4 (en) | 2009-11-11 |
HK1116929A1 (en) | 2009-01-02 |
EP1956669B1 (en) | 2010-12-15 |
CN101288196A (zh) | 2008-10-15 |
JP2007109576A (ja) | 2007-04-26 |
KR101345826B1 (ko) | 2013-12-30 |
CA2624684C (en) | 2011-02-08 |
KR20080048533A (ko) | 2008-06-02 |
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