WO2001029922A1 - Polymer electrolyte fuel cell - Google Patents
Polymer electrolyte fuel cell Download PDFInfo
- Publication number
- WO2001029922A1 WO2001029922A1 PCT/JP2000/007357 JP0007357W WO0129922A1 WO 2001029922 A1 WO2001029922 A1 WO 2001029922A1 JP 0007357 W JP0007357 W JP 0007357W WO 0129922 A1 WO0129922 A1 WO 0129922A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- conductive
- polymer electrolyte
- anode
- separator
- cathode
- 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
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01B—CABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
- H01B1/00—Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors
- H01B1/06—Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors mainly consisting of other non-metallic substances
- H01B1/12—Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors mainly consisting of other non-metallic substances organic substances
- H01B1/122—Ionic conductors
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01F—MAGNETS; INDUCTANCES; TRANSFORMERS; SELECTION OF MATERIALS FOR THEIR MAGNETIC PROPERTIES
- H01F1/00—Magnets or magnetic bodies characterised by the magnetic materials therefor; Selection of materials for their magnetic properties
- H01F1/01—Magnets or magnetic bodies characterised by the magnetic materials therefor; Selection of materials for their magnetic properties of inorganic materials
- H01F1/03—Magnets or magnetic bodies characterised by the magnetic materials therefor; Selection of materials for their magnetic properties of inorganic materials characterised by their coercivity
- H01F1/12—Magnets or magnetic bodies characterised by the magnetic materials therefor; Selection of materials for their magnetic properties of inorganic materials characterised by their coercivity of soft-magnetic materials
-
- 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
-
- 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
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0221—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
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0223—Composites
- H01M8/0226—Composites in the form of mixtures
-
- 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
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/1007—Fuel cells with solid electrolytes with both reactants being gaseous or vaporised
-
- 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 fuel cell using a polymer electrolyte, which is used for a portable power supply, a power supply for an electric vehicle, a home network: c system, and the like.
- Fuel cells using polymer electrolytes generate electricity and heat simultaneously by electrochemically reacting a fuel gas containing hydrogen with a fuel gas containing oxygen, such as air.
- This fuel cell basically consists of a pair of electrodes formed on both sides of a polymer electrolyte membrane that selectively transports hydrogen ions, that is, an anode and a force source.
- the electrode includes a catalyst layer mainly composed of carbon powder carrying a platinum group metal catalyst, and a diffusion layer formed on the outer surface of the catalyst layer and having both gas permeability and electronic conductivity.
- a gas sealing material and a gasket are placed around the electrodes so that the fuel gas and the oxidizing gas supplied to the electrodes do not leak out and the two types of gases do not mix with each other. Be placed.
- MEA electrolyte membrane-electrode assembly
- a conductive separation plate that mechanically secures the MEA and electrically connects adjacent MEAs to each other in series.
- a gas passage is formed in the part of the separator plate that comes into contact with the MEA to supply the reaction gas to the electrode surface and carry away the produced gas and surplus gas.
- the gas flow path can be provided separately from the separator plate. In general, a groove is formed on the surface of the substrate to form a gas flow path.
- the pipes for supplying the fuel gas and the oxidizing gas are branched into the number of separation plates to be used, and the branching destination is directly connected to the separation plate.
- a piping jig that connects to the groove of the evening board is required.
- This jig is called a manifold, and the type that connects directly from the fuel gas and oxidizing gas supply pipes as above is called an external manifold.
- an internal manifold There is a type of this manifold called an internal manifold that has a simpler structure.
- An internal manifold is one that has a through hole in a separator plate that has a gas flow path, through which the gas flow path enters and exits, and through which the fuel gas and oxidant gas are supplied directly. is there.
- Fuel cells generate heat during operation, so they need to be cooled with cooling water or the like to maintain the cells in a good temperature state.
- a cooling unit for flowing cooling water is provided for every one to three cells.
- the MEA, the separator, and the cooling section are alternately stacked, 10 to 200 cells are stacked, the stack is sandwiched between end plates via a current collector and an insulating plate, and both ends are fastened with fastening bolts.
- the structure of a general laminated battery is fixed from the beginning.
- the separator plate has high conductivity, is highly airtight with respect to fuel gas and oxidizing gas, and has high corrosion resistance to the reaction of redoxing hydrogen and oxygen. Need to have For this reason, conventional separation plates are usually made of carbon materials such as glass and expanded graphite, and the gas flow path is also cut on the surface, and in the case of expanded graphite, it is molded using a mold. It was produced by
- the metal plate is exposed to an oxidizing atmosphere having a pH of about 2 to 3 at a high temperature.
- the metal plate corrodes, the electrical resistance of the corroded portion increases, and the output of the battery decreases.
- the metal plate is dissolved, the dissolved metal ions diffuse into the polymer electrolyte and are trapped at the ion exchange site of the polymer electrolyte, resulting in a decrease in the ion conductivity of the polymer electrolyte itself. For these reasons, there was the problem that the power generation efficiency would gradually decrease if the battery was operated for a long time, using the metal plate as it was for the separation plate.
- the present invention provides a polymer electrolyte fuel cell provided with a novel conductive separator in order to solve the above problems.
- a polymer electrolyte fuel cell includes: a hydrogen ion conductive polymer electrolyte membrane; an anode and a force source sandwiching the hydrogen ion conductive polymer electrolyte membrane; and a fuel gas supplied to the anode.
- a cathode-side conductive separator having a gas flow path for supplying an oxidizing gas to the power source and a cathode-side conductive separator having a gas flow path for supplying an oxidizing gas to the power source.
- the conductive separator is made of a conductive airtight elastic body having acid resistance.
- the conductive hermetic elastic body has a main chain skeleton of polyisobutylene represented by the formula (1) or an ethylene propylene random copolymer represented by the formula (2); It is preferable that at least the inorganic conductive agent is mixed with the base material.
- X and Y are polymerizable functional groups, and m is an integer of 1 or more representing the number of repetitions of the isoptylene oligomer.
- X and Y are polymerizable functional groups, and 1, m and n are integers of 1 or more.
- FIG. 1 is a longitudinal sectional view of a main part showing a configuration of a MEA of a fuel cell according to an embodiment of the present invention.
- FIG. 2 is a front view of the separator used in the fuel cell according to the embodiment of the present invention, viewed from the cathode side.
- Fig. 3 is a rear view of the separation.
- FIG. 4 is a front view of another separation used in the fuel cell according to the embodiment of the present invention.
- FIG. 5 is a front view of the MEA sheet used in the fuel cell according to the example of the present invention.
- FIG. 6 is a diagram showing a time change of the output characteristics of the fuel cell according to the example of the present invention.
- the conductive separator is made of an acid-resistant conductive airtight elastic body.
- the conductive hermetic elastic body is preferably a polymer elastic body represented by the above formula (1) or (2), and a conductive material such as at least carbon powder or carbon fiber mixed with the matrix. Agent.
- This conductive hermetic elastic body is certainly made of glassy carbon or metal. Electric conductivity is lower than that of board.
- carbon paper that constitutes the porous electrode located outside the MEA is made of carbon paper. The conductive elastic material penetrates the surface, and the contact resistance between the separator and the MEA can be reduced.
- Separators made of a conductive airtight elastic material are unlikely to crack when vibrating under pressure, like a carbon plate. Furthermore, by selecting the base material and the conductive agent, there is no corrosion in an acidic atmosphere as in the case of metal plate separators.
- the present inventors have searched for a parent drug that satisfies the above requirements, and as a result, have found that the polyisobutylene represented by the above formula (1) or the ethylene propylene random copolymer represented by the formula (2) is a main chain bone. It has been found that high-grade elastomers are excellent in gas tightness, acid resistance and heat resistance and are particularly suitable as base materials for separation materials.
- the degree of polymerization of the polymer elastic body having the main chain skeleton represented by the formula (1) or (2) it is possible to realize the optimum elasticity for the separation of the polymer electrolyte fuel cell.
- a conductive agent such as acetylene black powder or graphite fiber is mixed, and the liquid material is cast into an appropriate mold, and cured by irradiating with an electron beam. Get.
- a sheet is made by injection molding the liquid. In this way, a sheet having a groove for supplying a fuel or oxidant gas can be continuously formed. Also in this respect, the processing for producing the separator can be greatly simplified compared to the conventional carbon and metal plates.
- the polymer represented by the above formula (1) is a polymer obtained by adding a terminal functional group X and Y to an isobutylene oligomer having a repeating number of m as one unit and cross-linking with a terminal functional group portion.
- X and Y are aryl group, acryloyl
- an aryl group, a methyl acryloyl group, an isocyanate group, or an epoxy group can be used. Since these functional groups are polyfunctional groups, if they are used as bridging points, the polymer after polymerization has a matrix structure crosslinked in a matrix form.
- the physical properties of the polymer having such a structure are greatly affected by the number of repetitions m of the isobutylene oligomer in the high molecular material represented by the formula (1), the overall degree of polymerization, and the type of the terminal functional group.
- the number of repetitions m of the isobutylene oligomer is 56 ⁇ m ⁇ 72, and the average is 64%. It is desirable that
- terminal functional groups X and Y of the isoptylene oligomer represented by the formula (1) are an aryl group, an acryloyl group, or a methyl acryloyl group, they are cured by electron beam irradiation.
- the terminal functional group is an isocyanate group, a urethane bond is formed by moisture, and when the terminal functional group is an epoxy group, the terminal is cured by heating using a known amine-based curing agent such as ethyldiamine.
- terminal functional groups X and Y of the ethylene propylene random copolymer represented by the formula (2) an acryloyl group, a methacryloyl group, an isocyanate group, an epoxy group and the like can be used.
- these polyfunctional groups are used as crosslinking points, a polymer having a network structure crosslinked in a matrix form is obtained.
- the physical properties of the polymer are greatly influenced by 1, m and n in the formula (2), the overall degree of polymerization 1 + m + n, and the type of the terminal functional group.
- 1 and m are 2, 0000 to: 15, 5,000, and n is 100.
- the degree of polymerization is preferably about 500, and the degree of polymerization 1 + m + n is preferably 5,000 to 20,000.
- electron beam irradiation as in the case of the isobutylene oligomer represented by the formula (1), Crosslinking can be achieved by urethane bonding with moisture or curing reaction by heating using an amine-based curing agent.
- conductive powder conductive carbon powder, fiber, and silver powder are preferably used.
- the mixing ratio of the base material and the inorganic conductive agent is suitably in the range of 90 to 30 wt% of the former and 10 to 70 wt% of the latter.
- the amount of the inorganic conductive agent is less than 10 wt%, the electric resistance is high, and when the amount of the inorganic conductive agent exceeds 70 wt%, the composition does not cure.
- FIG. 1 is a longitudinal sectional view showing the configuration of the MEA.
- Reference numeral 11 denotes a diffusion layer made of carbon paper, and reference numeral 12 denotes a catalyst layer formed on one surface of the diffusion layer.
- MEA 15 is constituted by the pair of electrodes with the polymer electrolyte membrane 14 interposed therebetween.
- FIG. 2 is a front view of the conductive separator viewed from the cathode side
- FIG. 3 is a rear view of the conductive separator seen from the anode side.
- the conductive separator 20 serves as both a cathode-side conductive separator and an anode-side conductive separator.
- Separator 20 has, at one end, an oxidant gas supply side through hole 23a, a fuel gas supply side through hole 24a, and a cooling water supply side through hole 25a. At the end, there are an oxidant gas discharge side through hole 23b, a fuel gas discharge side through hole 24b, and a cooling water discharge side through hole 25b.
- a groove 26 which continues from the through holes 23a to 23b, and a rib 27 partitioning the center and a plurality of parallel gas flows are formed in this groove.
- a rib group 28 for forming the path 29 is provided.
- the surface of the separator 20 facing the anode has a through hole 24a.
- a groove 30 is formed following the ribs 24b, and a rib 31 for partitioning the center and a rib group 32 for forming a plurality of parallel gas flow paths 33 are provided in this groove.
- the conductive separator 20 shown here is inserted between the cells, and the separator on the cathode side located at the end of the stacked battery in which a plurality of cells are stacked is connected to one surface. Has a gas flow path as shown in FIG. 2, but the other surface is flat. Further, the separator on the anode side located at the end of the stacked battery has a gas flow path as shown in FIG. 3, but the other surface is flat.
- Fig. 4 is a front view of a surface having a cooling water flow path of the conductive separator.
- the conductive separator 41 like the separator 20, has an oxidizing agent at one end.
- It has a gas supply side through hole 43a, a fuel gas supply side through hole 44a and a coolant supply side through hole 45a, and the other end has an oxidant gas discharge side. It has a through hole 43b, a fuel gas discharge side throughhole 44b, and a cooling water discharge side throughhole 45b. On one surface of the separator 41, there is formed a groove 46 that forms a flow path for cooling water and extends from the through holes 44a to 44b, and a plurality of circular ribs 4 are formed in this groove. 7 are provided.
- the conductive separator 41 is joined to the pair with the surfaces having the cooling water passages 46 facing each other, and forms a cooling unit for flowing the cooling water between the two.
- An oxidizing gas flow path is formed on the back surface of one separator, and a fuel gas flow path is formed on the back surface of the other separator.
- FIG. 5 is a front view of the MEA.
- the MEA 50 is composed of a polymer electrolyte membrane 51 and an electrode 52 sandwiching the polymer electrolyte membrane 51.
- the polymer electrolyte membrane 51 has, at one end, a supply-side through-hole 53a for oxidant gas and fuel gas.
- Supply-side through-hole 54a and cooling-water supply-side through-hole 55a, and the other end has an oxidant gas discharge-side through-hole 53b It has a hole 54b and a cooling water discharge side through hole 55b.
- the MEA 50 shown in FIG. 5 is laminated via a separator 20 and a pair of separators 41 forming the above-described cooling unit is inserted for every two cells. 50 cells were stacked.
- a gasket having a pair of through holes for oxidizing gas, fuel gas, and cooling water is provided between the electrolyte membrane 51 and the conductive separator so as to surround the electrode 52. Intervened.
- Example 1 Example 1
- Platinum particles having an average particle size of about 30 A were supported on acetylene black powder, and the weight ratio of acetylene black to platinum was 3: 1.
- This catalyst powder was dispersed in isopropanol. This dispersion was mixed with an ethyl alcohol dispersion of perfluorocarbon sulfonic acid powder represented by the formula (3) to prepare a catalyst paste.
- the number of repetitions m of the isobutylene oligomer represented by the formula (1) is set to an average of 64 in the range of 56 to 72, 100 g of a liquid raw material in which the functional groups X and Y are both aryl groups, and acetylene black 50
- 50 g of fibrous graphite (average diameter 50 / xm, average length 0.5 mm) and 200 g of viscosity-adjusting methyl ethyl ketone are added, and mixed well to obtain a stock solution for separation.
- This undiluted solution was poured into a stainless steel mold and stored for 1 hour in a reduced pressure atmosphere at 50 to 0.2 atm to volatilize methylethylketone.
- an electron beam was irradiated at an accelerating voltage of 500 keV and an irradiation dose of 50 Mrad to polymerize the terminal aryl group of the isobutylene oligomer, thereby producing a conductive sheet.
- the degree of polymerization is about 10, 00 Met.
- the sheet after polymerization became stiff, and the contact resistance with MEA could not be reduced unless the tightening pressure during battery assembly was increased. Also, if 111 was larger than 72, it was too soft, and the gas flow channel formed on the separator surface was crushed by the tightening pressure during battery assembly. As a result of examining the effect of the degree of polymerization by controlling the amount of electron beam irradiation, if the degree of polymerization is smaller than 50,000, the sheet is too soft and the grooves in the gas flow channel are crushed in the same manner as described above. Was.
- Separation size 20 is 10 cm x 20 cm, thickness is 4 mm, grooves 26 and 30 are 1.5 mm deep, ribs 28 and 32 are 1 mm wide The width of the gas channels 29 and 33 between these ribs is 2 mm.
- Separation area 41 is the same size as separation area 20, and the depth of groove 46, which is the cooling water channel, is 1.5 mm.
- FIG. 5 through holes for oxidizing gas, fuel gas and cooling water flow were formed in the proton conductive polymer electrolyte membrane of MEA prepared above.
- a battery stack was assembled by combining 50 of the MEAs with the conductive separators 20 and 41 described above. At both ends of the battery stack, a stainless steel current collector plate, an insulating plate made of an electrically insulating material, and an end plate were overlapped and fixed with a fastening rod.
- the clamping pressure was separator evening area equivalent or 4 kgf Bruno cm 2.
- Fastening is compared with the conventional fuel cell using a separator consisting of a pressure plate, which required a high fastening pressure of about 20 kgf / cm2.
- the polymer electrolyte fuel cell of this example thus produced was held at 85 :, and the anode was humidified and heated to have a dew point of 83, and the cathode was charged at a dew point of 78. Humidified and heated air was supplied so that As a result, a battery open-circuit voltage of 50 V was obtained at no load when no current was output to the outside.
- the battery of this example had a configuration in which MEA was sandwiched between elastic separators, it was particularly resistant to vibration and impact.
- a battery made of a conventional carbon separator was dropped from a height of 2 m, cracks were formed in the separator over about 10 times on average. Even after the drop test of about 100 times, the battery of this example showed no irreparable damage except for the loosening of the rod at the fastening portion.
- a polymer elastic body having an ethylene propylene random copolymer represented by the formula (2) as a main chain skeleton is used as a base material. Then, a mixture obtained by mixing inorganic conductivity with this was used.
- the degree of polymerization of the oligomer was larger than 200,000, the sheet was too hard, and the contact resistance with MEA could not be reduced unless the tightening pressure during battery assembly was increased. Further, when the degree of polymerization was smaller than 4.0000, it was too soft, and the gas flow grooves formed on the surface of the separator were crushed by the tightening pressure during battery assembly. As a result of examining the effect of the degree of polymerization by controlling the amount of electron beam irradiation, when the degree of polymerization was smaller than 50,000, the sheet was too soft and the gas flow grooves were crushed in the same manner as described above.
- Example 2 Using the separator made of this conductive sheet, a battery similar to that of Example 1 was assembled, and the characteristics were evaluated under the same conditions as Example 1. As a result, it was confirmed that the battery of the present example also had excellent characteristics like the battery of Example 1. The anti-vibration and anti-shock properties were also excellent as in the battery of Example 1. Industrial applicability
- a significant cost reduction can be achieved by using a conductive airtight elastic body having acid resistance instead of the conventional carbon plate cutting method as a separation. Furthermore, it has excellent vibration and shock resistance, and is particularly suitable as a power source for electric vehicles.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- General Chemical & Material Sciences (AREA)
- Electrochemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Sustainable Energy (AREA)
- Sustainable Development (AREA)
- Life Sciences & Earth Sciences (AREA)
- Physics & Mathematics (AREA)
- Composite Materials (AREA)
- Spectroscopy & Molecular Physics (AREA)
- Dispersion Chemistry (AREA)
- Power Engineering (AREA)
- Fuel Cell (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
Claims
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP00969973A EP1248310A4 (en) | 1999-10-21 | 2000-10-20 | POLYMERELEKTROLYBRENNSTOFFZELLE |
| US10/111,261 US7008714B1 (en) | 1999-10-21 | 2000-10-20 | Polymer electrolyte fuel cell |
| JP2001531168A JP3970027B2 (ja) | 1999-10-21 | 2000-10-20 | 高分子電解質型燃料電池 |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11/299646 | 1999-10-21 | ||
| JP29964699 | 1999-10-21 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| WO2001029922A1 true WO2001029922A1 (en) | 2001-04-26 |
| WO2001029922A9 WO2001029922A9 (en) | 2002-02-28 |
Family
ID=17875283
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/JP2000/007357 Ceased WO2001029922A1 (en) | 1999-10-21 | 2000-10-20 | Polymer electrolyte fuel cell |
Country Status (6)
| Country | Link |
|---|---|
| US (1) | US7008714B1 (ja) |
| EP (1) | EP1248310A4 (ja) |
| JP (1) | JP3970027B2 (ja) |
| KR (1) | KR100417050B1 (ja) |
| CN (1) | CN1183619C (ja) |
| WO (1) | WO2001029922A1 (ja) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003317793A (ja) * | 2002-04-23 | 2003-11-07 | Hitachi Ltd | 固体高分子型燃料電池及びそれを用いた発電システム |
| JP2005529466A (ja) * | 2002-06-05 | 2005-09-29 | ゼネラル・モーターズ・コーポレーション | ステンレス鋼製二極式プレートプレートのためのAu超低積載 |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE10307278B4 (de) | 2003-02-20 | 2008-03-27 | Staxera Gmbh | Brennstoffzellenstapel |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59188673U (ja) * | 1983-06-01 | 1984-12-14 | 工業技術院長 | 燃料電池 |
| JPS6065405A (ja) * | 1983-09-19 | 1985-04-15 | 株式会社富士電機総合研究所 | シ−ト状弾性導電板 |
| JPH07102017A (ja) * | 1993-10-07 | 1995-04-18 | Kanegafuchi Chem Ind Co Ltd | 末端に官能基を有する重合体及びその製造方法 |
| WO1999005737A1 (en) * | 1997-07-28 | 1999-02-04 | Nisshinbo Industries, Inc. | Separator for fuel cells |
Family Cites Families (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1495275A (en) * | 1974-06-04 | 1977-12-14 | Exxon Research Engineering Co | Conductive polyolefin compositions |
| US4124747A (en) * | 1974-06-04 | 1978-11-07 | Exxon Research & Engineering Co. | Conductive polyolefin sheet element |
| US4758631A (en) * | 1986-10-16 | 1988-07-19 | Dow Corning Corporation | Method of preparing allyl-terminated polyisobutylene |
| JPS6454607A (en) | 1987-08-25 | 1989-03-02 | Nec Corp | Electric conductive compound sheet |
| US5110691A (en) * | 1991-01-16 | 1992-05-05 | International Fuel Cells Corporation | Fuel cell component sealant |
| EP0529102B1 (en) * | 1991-03-15 | 1998-10-28 | Tonen Corporation | Terminally modified polyolefin |
| JPH06333580A (ja) | 1993-05-19 | 1994-12-02 | Mitsubishi Heavy Ind Ltd | 燃料電池用セパレータ |
| JP3353567B2 (ja) * | 1995-09-29 | 2002-12-03 | 松下電器産業株式会社 | 燃料電池 |
| JPH11219714A (ja) * | 1998-02-03 | 1999-08-10 | Matsushita Electric Ind Co Ltd | 燃料電池 |
| WO1999053559A1 (fr) * | 1998-04-14 | 1999-10-21 | Three Bond Co., Ltd. | Materiau d'etancheite pour pile a combustible |
| EP1009052B1 (en) * | 1998-06-02 | 2012-02-15 | Panasonic Corporation | Polymer electrolyte fuel cell and method of manufacture thereof |
| JP3640333B2 (ja) | 1998-06-02 | 2005-04-20 | 松下電器産業株式会社 | 高分子電解質型燃料電池 |
| JP3951484B2 (ja) * | 1998-12-16 | 2007-08-01 | トヨタ自動車株式会社 | 燃料電池 |
-
2000
- 2000-10-20 CN CNB008144982A patent/CN1183619C/zh not_active Expired - Fee Related
- 2000-10-20 KR KR10-2002-7004938A patent/KR100417050B1/ko not_active Expired - Fee Related
- 2000-10-20 US US10/111,261 patent/US7008714B1/en not_active Expired - Fee Related
- 2000-10-20 JP JP2001531168A patent/JP3970027B2/ja not_active Expired - Fee Related
- 2000-10-20 EP EP00969973A patent/EP1248310A4/en not_active Withdrawn
- 2000-10-20 WO PCT/JP2000/007357 patent/WO2001029922A1/ja not_active Ceased
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59188673U (ja) * | 1983-06-01 | 1984-12-14 | 工業技術院長 | 燃料電池 |
| JPS6065405A (ja) * | 1983-09-19 | 1985-04-15 | 株式会社富士電機総合研究所 | シ−ト状弾性導電板 |
| JPH07102017A (ja) * | 1993-10-07 | 1995-04-18 | Kanegafuchi Chem Ind Co Ltd | 末端に官能基を有する重合体及びその製造方法 |
| WO1999005737A1 (en) * | 1997-07-28 | 1999-02-04 | Nisshinbo Industries, Inc. | Separator for fuel cells |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003317793A (ja) * | 2002-04-23 | 2003-11-07 | Hitachi Ltd | 固体高分子型燃料電池及びそれを用いた発電システム |
| JP2005529466A (ja) * | 2002-06-05 | 2005-09-29 | ゼネラル・モーターズ・コーポレーション | ステンレス鋼製二極式プレートプレートのためのAu超低積載 |
Also Published As
| Publication number | Publication date |
|---|---|
| KR20020062733A (ko) | 2002-07-29 |
| JP3970027B2 (ja) | 2007-09-05 |
| CN1183619C (zh) | 2005-01-05 |
| US7008714B1 (en) | 2006-03-07 |
| WO2001029922A9 (en) | 2002-02-28 |
| CN1379918A (zh) | 2002-11-13 |
| EP1248310A4 (en) | 2006-11-22 |
| EP1248310A1 (en) | 2002-10-09 |
| KR100417050B1 (ko) | 2004-02-05 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP4036754B2 (ja) | 高分子電解質型燃料電池 | |
| KR100372926B1 (ko) | 고분자전해질형연료전지 및 그 제조방법 | |
| CN1186840C (zh) | 高分子电解质型燃料电池及其制造方法 | |
| US7014940B2 (en) | High-polymer electrolyte fuel cell | |
| CN1416604A (zh) | 高分子电解质型燃料电池及其制造方法 | |
| JP3640333B2 (ja) | 高分子電解質型燃料電池 | |
| JP2004327358A (ja) | 固体高分子型燃料電池 | |
| WO2003081707A1 (en) | Electrolyte membrane/electrode union for fuel cell and process for producing the same | |
| CN1462489A (zh) | 燃料电池用电极及其制造方法 | |
| JP2003297385A (ja) | 燃料電池セパレータの製造方法、燃料電池セパレータ、および固体高分子型燃料電池 | |
| JP4561239B2 (ja) | 燃料電池セパレータおよびそれを用いた燃料電池 | |
| WO2001029922A1 (en) | Polymer electrolyte fuel cell | |
| JP2002208412A (ja) | 高分子電解質型燃料電池 | |
| JP4781333B2 (ja) | 高分子電解質型燃料電池 | |
| JPWO2001029922A1 (ja) | 高分子電解質型燃料電池 | |
| US20240055621A1 (en) | Fuel cell stack and production method | |
| JP2008010431A5 (ja) | ||
| JP4508574B2 (ja) | 燃料電池用セパレータ、燃料電池用セパレータの製造方法 | |
| JP4274892B2 (ja) | 高分子電解質型燃料電池 | |
| JP2005108777A (ja) | 燃料電池用セパレータおよびこれを用いた燃料電池 | |
| JP2004192878A (ja) | 固体高分子型燃料電池用セパレータ材の製造方法 |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| AK | Designated states |
Kind code of ref document: A1 Designated state(s): CN JP KR US |
|
| AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE |
|
| DFPE | Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101) | ||
| 121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
| AK | Designated states |
Kind code of ref document: C2 Designated state(s): CN JP KR US |
|
| AL | Designated countries for regional patents |
Kind code of ref document: C2 Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE |
|
| COP | Corrected version of pamphlet |
Free format text: PUBLISHED CLAIMS AND AMENDED CLAIMS (3 PAGES) REPLACED BY CORRECT CLAIMS AND AMENDED CLAIMS (5 PAGES) |
|
| ENP | Entry into the national phase |
Ref country code: JP Ref document number: 2001 531168 Kind code of ref document: A Format of ref document f/p: F |
|
| WWE | Wipo information: entry into national phase |
Ref document number: 008144982 Country of ref document: CN Ref document number: 1020027004938 Country of ref document: KR |
|
| WWE | Wipo information: entry into national phase |
Ref document number: 10111261 Country of ref document: US |
|
| WWE | Wipo information: entry into national phase |
Ref document number: 2000969973 Country of ref document: EP |
|
| WWP | Wipo information: published in national office |
Ref document number: 1020027004938 Country of ref document: KR |
|
| WWP | Wipo information: published in national office |
Ref document number: 2000969973 Country of ref document: EP |
|
| WWG | Wipo information: grant in national office |
Ref document number: 1020027004938 Country of ref document: KR |