WO2006118107A1 - 燃料電池および燃料電池用触媒層電極 - Google Patents
燃料電池および燃料電池用触媒層電極 Download PDFInfo
- Publication number
- WO2006118107A1 WO2006118107A1 PCT/JP2006/308646 JP2006308646W WO2006118107A1 WO 2006118107 A1 WO2006118107 A1 WO 2006118107A1 JP 2006308646 W JP2006308646 W JP 2006308646W WO 2006118107 A1 WO2006118107 A1 WO 2006118107A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- fuel cell
- catalyst layer
- layer electrode
- solid electrolyte
- electrolyte membrane
- Prior art date
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/8605—Porous electrodes
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/90—Selection of catalytic material
- H01M4/92—Metals of platinum group
- H01M4/925—Metals of platinum group supported on carriers, e.g. powder carriers
- H01M4/926—Metals of platinum group supported on carriers, e.g. powder carriers on carbon or graphite
-
- 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
- H01M8/1009—Fuel cells with solid electrolytes with one of the reactants being liquid, solid or liquid-charged
- H01M8/1011—Direct alcohol fuel cells [DAFC], e.g. direct methanol fuel cells [DMFC]
-
- 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 planar fuel cell effective for the operation of an electronic device exhibiting stable and good characteristics, a fuel cell for replenishing the fuel cell with liquid fuel and water, and a catalyst layer electrode for the fuel cell About.
- Fuel cells are attracting attention as a clean power generation system in which the product of the cell reaction is water in principle and has almost no adverse effect on the global environment.
- the direct methanol fuel cell (DMFC) that has a solid electrolyte membrane and uses liquid fuel is expected to be put to practical use as a fuel cell suitable for portable information devices.
- the DMFC described in Japanese Patent No. 3413111 reacts with a solid electrolyte membrane having proton conductivity, a catalyst layer electrode having catalyst-supported carbon fine particles coated with an ion exchange resin, and a catalyst layer electrode.
- a gas diffusion layer that supplies fuel and collects electric charge, and generates an electric charge and proton from the fuel and water, a catalyst layer electrode having catalyst-supported carbon fine particles coated with the ion exchange resin, and a catalyst Membrane Electrode Assembly (MEA) consisting of a gas diffusion layer that supplies oxygen to the layer electrode and conducts charge, and is composed of protons and a force sword that generates water from oxygen, is used as a unit cell.
- MEA catalyst Membrane Electrode Assembly
- the catalyst layer electrode there are voids composed of fine pores formed between secondary particles or tertiary particles of carbon fine particles, and function as a reaction gas diffusion path.
- DMFC has developed a solid electrolyte membrane with high ionic conductivity, and uses catalyst-supported carbon fine particles coated with an ion exchange resin of the same or different type as the solid electrolyte membrane as a constituent material of the electrode catalyst layer.
- the power generation performance has been greatly improved due to the three-dimensionalization of the reaction sites in the catalyst layer.
- the corner 13 of the electrode is easily peeled off from the solid electrolyte membrane 11, and the area that can contribute to the power generation reaction is reduced, so that sufficient power generation performance cannot be obtained.
- the catalyst layer electrode 12 is made of a felt material such as carbon paper or carbon fiber, and is bonded to the solid electrolyte membrane 11 by a laminating process using a hot press. Therefore, it may peel off from the corner 13 when it is installed in the battery body. For this reason, there is a problem in that the reaction that should be originally performed between the catalyst layer electrode 12 and the solid electrolyte membrane 11 is not performed, battery characteristics are partially inhibited, and an output as designed cannot be obtained.
- the present invention has been made to solve the above-mentioned problems, and has a fuel cell and a fuel cell catalyst having a stable and good battery performance in which the pressure-bonded catalyst layer electrode is hardly peeled off from the solid electrolyte membrane.
- An object is to provide a layer electrode.
- a fuel cell according to the present invention includes a solid electrolyte membrane, an anode and a force sword that are provided to face each other with the solid electrolyte membrane interposed therebetween, and a single unit cell or a plurality of unit cells are arranged in a plane direction.
- at least one of the anode and force sword catalyst layer electrodes does not have a corner of 90 ° or less, and is integrated with each surface of the solid electrolyte membrane. It is characterized by being.
- Each of the catalyst layer electrodes of the anode and the force sword has a substantially rectangular shape in two-dimensional projection plane, and ends of adjacent sides in at least one corner meet at an angle of 90 ° or less. It has a missing corner part in which a part of the corner part is missing so as not to be pressed, and is crimped to each surface of the solid electrolyte membrane.
- the catalyst layer electrode for a fuel cell according to the present invention comprises a solid electrolyte membrane, an anode and a force sword provided to face each other with the solid electrolyte membrane interposed therebetween as a unit cell, and the unit cell is a single or a surface.
- a catalyst layer electrode for a fuel cell according to the present invention is a catalyst layer electrode used in the fuel cell described above, and has a two-dimensional projection surface shape that is substantially rectangular, and is adjacent in a corner portion. It is characterized by having a missing corner portion in which a part of the corner portion is missing so that the ends of the sides do not meet at an angle of 90 ° or less.
- the two-dimensional projection surface shape of the catalyst layer electrode is a pentagon or more polygon, or the two-dimensional projection surface shape of the corner portion of the catalyst layer electrode is an arc.
- the corner is an angle exceeding 90 ° (obtuse angle) and that the area is 90% or more of the area of a true rectangle that does not have a missing corner on the two-dimensional projection plane.
- the radius of curvature R of the arc at the corner is set to 1 mm or more, and the area of 90% or more of the area of the true rectangular shape having no missing corner on the two-dimensional projection plane is assumed. Is desirable.
- the missing corner portion is a triangular shape having, as a vertex, an intersection where the ends of adjacent sides meet on the two-dimensional projection plane, and a straight line that obliquely crosses the adjacent sides at a predetermined distance from the intersection. It may be formed by cutting away the part (Fig. 2), and the adjacent sides are separated by a predetermined length from the intersection where the ends of the adjacent sides meet on the two-dimensional projection plane. It may be formed by cutting away the outer part of the circumscribed arc (Fig. 3). Such a missing corner portion is formed by chamfering or cutting the corner portion of the true rectangular catalyst layer electrode shown in FIG.
- the present invention also includes a catalyst layer electrode having a shape that does not lose corner portions.
- a catalyst layer electrode having a shape that does not lose corner portions.
- each side of the catalyst layer electrode has a curved shape that curves outward (bulges) on the two-dimensional projection plane, the ends of adjacent sides always meet at an angle of more than 90 ° (Fig. Four).
- Various two-dimensional curves such as a perfect circular arc, an elliptical arc, a catenary line, a cycloid, and a cardioid can be used for the curved shape of the side. Even in the case of a catalyst layer electrode having such a curved side, the effect can be further enhanced if the corners are further omitted (FIG. 5).
- multiple solid-phase electrolysis with multiple catalyst layer electrodes of the same size and shape A multi-type membrane / electrode assembly may be formed by attaching to a membrane (FIGS. 6 and 7).
- the catalyst layer electrode can be obtained by integrally forming a sheet-like carbon-containing base material coated or impregnated with a catalyst-containing substance by pressure bonding. Specifically, for example, it can be pressure-bonded to the solid electrolyte membrane by hot pressing at a temperature of 100 to 160 ° C.
- a felt sheet such as carbon fiber or carbon paper is used for the carbon-containing substrate, and such a sheet is impregnated with or impregnated with a predetermined component and amount of catalyst-containing paste, and a solid electrolyte membrane is sandwiched therebetween.
- a paste application sheet is attached to both sides, and this is integrally molded and crimped with a heat press.
- FIG. 1 is a side sectional view schematically showing the structure of a fuel cell.
- FIG. 2 is a plan view showing a catalyst layer electrode of Example 1.
- FIG. 3 is a plan view showing a catalyst layer electrode of Example 2.
- FIG. 4 is a plan view showing a catalyst layer electrode of Example 3.
- FIG. 5 is a plan view showing a modified catalyst layer electrode.
- FIG. 6 is a plan view showing a multi-type membrane electrode assembly having multipolar catalyst layer electrodes.
- FIG. 7 is a plan view showing a catalyst layer electrode of Example 4.
- FIG. 8 is a plan view showing a catalyst layer electrode of Comparative Example 2.
- FIG. 9 is a plan view showing a catalyst layer electrode of Comparative Example 1.
- FIG. 10 is a side view showing a catalyst layer electrode that is hot-press bonded to a solid electrolyte membrane of a conventional fuel cell.
- the fuel cell 1 is entirely covered with a protective cover 20 and has a unit cell inside.
- the fuel cell 1 is connected to the inner side of the protective cover 20 through the sealing members 17 and 18.
- the unit cell is integrated by tightening with a bolt 28 and a nut 29.
- Various spaces and gaps are formed inside the fuel cell 1 by the sealing members 17 and 18 as the pressing members and the plurality of spacers 25.
- the cathode side space is used as the water storage chamber 26, and the anode side space is used as the fuel storage chamber 27.
- a plurality of fine ventilation holes 24 are formed in the protective cover 20 on the force sword side and communicate with the space portions 26, respectively.
- a unit cell of the fuel cell includes a solid electrolyte membrane 11, an anode, and a force sword.
- the anode and the force sword are opposed to each other with the solid electrolyte membrane 11 interposed therebetween.
- the anode has an anode catalyst layer electrode 12A (12B to 12D) and an anode gas diffusion layer 14.
- the anode catalyst layer electrode 12A (12B to 12D) is used to oxidize the fuel supplied through the gas diffusion layer 14 and extract electrons and protons from the fuel.
- the catalyst layer electrode 12A (12B to 12D) ) And the gas diffusion layer 14 are stacked.
- the anode catalyst layer electrode 12A (12B to 12D) is made of, for example, carbon powder containing a catalyst.
- the catalyst examples include platinum (Pt) fine particles, iron (Fe), nickel (Ni), cobalt (Co), ruthenium (Ru), molybdenum (Mo) and other transition metals or oxides thereof or alloys thereof. Fine particles such as are used. However, it is preferable that the catalyst is made of an alloy of noretenium and platinum, because inactivation of the catalyst due to adsorption of carbon monoxide (CO) can be prevented.
- the anode catalyst layer electrode 12A (12B to 12D) includes fine particles of resin used for the solid electrolyte membrane 11 described later. This is to facilitate the movement of the generated protons.
- the gas diffusion layer 14 is made of, for example, a thin film made of a porous carbon material, and specifically made of carbon paper or carbon fiber. Note that a negative electrode lead 16b that conducts to the end of the gas diffusion layer 14 extends outward.
- the force sword has force sword catalyst layer electrodes 12A (12B to 12D) and a force sword gas diffusion layer 15.
- the force sword catalyst layer electrode 12A (12B ⁇ : 12D) reduces oxygen and reacts the electrons with the proton generated in the anode catalyst layer electrode 12A (12B ⁇ : 12D) to generate water.
- the anode catalyst layer electrode 12A (12B to 12D) and the gas diffusion layer 14 are configured in the same manner. In other words, the force sword is applied in order from the solid electrolyte membrane 11 side.
- a force sword catalyst layer electrode 12A (12B to 12D) made of carbon powder containing a catalyst and a force sword gas diffusion layer 15 (gas permeable layer) made of a porous carbon material are stacked.
- the catalyst used in the force sword catalyst layer electrode 12A (12B to 12D) is the same as that of the anode catalyst layer electrode 12A (12B to 12D), and the anode catalyst layer electrode 12A (12B to 12D) is a solid electrolyte membrane 11 It is the same as the anode catalyst layer electrode 12A (12B to: 12D) that the resin fine particles used in the above may be included.
- a positive electrode lead 16a connected to the end of the force sword gas diffusion layer 15 extends outward.
- the shape of the catalyst layer electrode is, for example, as shown in FIG. 2 in which the shape of the two-dimensional projection surface of the catalyst layer electrode 12A is a pentagon or more polygon, or the shape of the catalyst layer electrode 12B as shown in FIG.
- the two-dimensional projection surface shape of the corner portion 13B can be an arc.
- the corners have an obtuse angle of 90 ° or more and have an area of 90% or more of the area of a true rectangular shape having no missing corners on the two-dimensional projection plane.
- the radius of curvature R of the corner arc is set to lmm or more, and the area is 90% or more of the area of the true rectangular shape with no corners missing from the two-dimensional projection plane. I hope it will be something. If the chamfer is excessively large or the radius of curvature of the arc is excessively large, the area of the catalyst layer electrode itself may become too small, and the reaction area required for power generation may be insufficient. . If it is 90% or more of the original rectangular area, there is virtually no possibility of this.
- the missing corner portion 13A has, as a vertex, an orthogonal point where adjacent side ends meet on the two-dimensional projection plane, and each adjacent side at a predetermined length away from the orthogonal point. You may make it form by cutting out the triangular part which makes the base the straight line crossing diagonally.
- the missing corner portion 13B is formed by cutting away the outer part of the arc where the adjacent sides circumscribe each other at a predetermined distance from the orthogonal point where the adjacent side ends meet on the two-dimensional projection plane. You may make it form.
- Such a missing corner is formed by chamfering or cutting a corner of the true rectangular catalyst layer electrode shown in FIG.
- a catalyst layer electrode having a shape that does not lose corner portions can be included in the present invention.
- each side 12a, 12b of the catalyst layer electrode 12C is connected to the two-dimensional projection plane. If the curved shape curves outward (bulges out), the ends of adjacent sides will always meet at an angle exceeding 90 °.
- Various two-dimensional curves such as a perfect circular arc, an elliptical arc, a catenary line, a cycloid, and a cardioid can be used as the side curve shape.
- FIG. 5 even in the catalyst layer electrode 12D having curved sides 12a and 12b, the effect can be further enhanced if the corner portion is formed by missing the corner portion.
- the solid electrolyte membrane 11 is used to transport the proton generated in the anode catalyst layer electrode 12A (12B to 12D) to the force sword catalyst layer electrode 12A (12B to 12D). It is made of a material that has no conductivity and can transport protons. For example, it is composed of a polyperfluorosulfonic acid resin membrane, specifically, a naphthoion membrane manufactured by DuPont, a Flemion membrane manufactured by Asahi Glass, or an aciplex membrane manufactured by Asahi Kasei Kogyo.
- a solid electrolyte membrane 11 capable of transporting protons such as a hydrogen-based resin may be configured.
- a plurality of catalyst layer electrodes may be arranged in parallel on one solid electrolyte membrane 11 so as to form a multi-type membrane electrode assembly.
- four catalyst layer electrodes El, E2, E3, and E4 are arranged in parallel in the width direction (X direction) at equal pitch intervals.
- catalyst layer electrodes E1 to E4 catalyst layer electrodes 12B having R chamfered corner portions 13B shown in FIG. 3 and having an aspect ratio of 3 to 8 were used.
- a fuel storage chamber 27 having a liquid fuel storage space formed therein is provided adjacent to the anode gas diffusion layer 14. Yes.
- the use of high-concentration liquid fuel has the advantage that the volume efficiency of the fuel cell is improved and the size and weight of the fuel cartridge carried with the fuel cell can be kept small.
- a fuel supply port (not shown) penetrating the seal member 18 communicates with the fuel storage chamber 27 so that liquid fuel is supplied to the fuel storage chamber 27.
- a lid (not shown) for closing the fuel supply port 21 is detachably attached to the fuel supply port.
- the fuel storage chamber 27 and the lid body are hard materials that do not swell with liquid fuel such as polytetrafluoroethylene, polystyrene, polypropylene, or polycarbonate. Made of quality plastic.
- the fuel storage chamber 27 and the lid can be made of a metal material having excellent corrosion resistance such as stainless steel and nickel metal.
- the fuel storage chamber 27 is not arranged to prevent short circuit between the anode catalyst layer electrode 12A and the force sword catalyst layer electrode 12A or not shown for preventing short circuit. It is necessary to insert an insulating member.
- the negative electrode lead 16b has a large number of openings and gaps and has a shape that does not hinder gas diffusion.
- the fuel storage chamber 27 may be filled with a liquid fuel-impregnated member that is impregnated and held with liquid fuel.
- a liquid fuel-impregnated member for example, porous polyester fiber, specifically, UNIVEX manufactured by Unitica is used.
- This liquid fuel impregnation section is disposed between the anode gas diffusion layer 14 and the fuel opening (not shown), and has a function of supplying an appropriate amount of fuel to the anode.
- polyester fiber it is made of a material that can hold liquid by utilizing the liquid permeability, such as sponge or fiber aggregate, which may be made of various water-absorbing polymers such as acrylic resin. .
- This liquid fuel impregnation part is effective for supplying an appropriate amount of fuel regardless of the posture of the main body.
- liquid fuel examples include methanol aqueous solution, ethanol aqueous solution, propanol fuel such as propanol aqueous solution and pure propanol, Daricol fuel such as glycol aqueous solution and pure glycol, dimethyl ether, formic acid aqueous solution, sodium formate aqueous solution, acetic acid aqueous solution, ethylene glycol
- An organic aqueous solution containing hydrogen such as an aqueous solution is used.
- an aqueous methanol solution is preferable because it has carbon number of 1 and carbon dioxide is generated during the reaction, and can generate electricity at a low temperature and can be produced relatively easily from industrial waste. .
- liquid fuel suitable for the fuel cell is used.
- the protective bar 20 on the force sword side has a large number of vent holes 24 for supplying outside air to the force sword gas diffusion layer 15 by natural diffusion through a gap, for example. These vent holes 24 form an opening through which the outside air passes, but can prevent the entry or contact of minute or needle-like foreign matters to the force sword gas diffusion layer 15 from the outside without obstructing the passage of the outside air.
- the shape is devised [0031] Although various embodiments have been described above, the present invention is not limited to the above-described embodiments, and various modifications and combinations can be made.
- Example 1 is a catalyst layer electrode 12A having the shape shown in FIG. 2
- Example 2 is a catalyst layer electrode 12B having the shape shown in FIG. 3
- Example 3 is a catalyst layer electrode 12C having the shape shown in FIG. 4, and Comparative Example 1 shows the results obtained using the catalyst layer electrodes 12 having the shapes shown in FIG.
- the length L1 of the long side 12b is 40 mm
- the length L2 of the short side 12a is 30 mm
- the chamfer size L3 of the missing corner 13A in Example 1 is lmm
- the missing corner 13B in Example 2 the radius of curvature R3 of the short side 12a was set to 100 mm
- the radius of curvature R1 of the long side 12b was set to 200 mm.
- each of Examples 1, 2, 3 and Comparative Example 1 was hot pressed under the conditions of a temperature of 125 ° C. and a pressure of 300 MPa / cm 2 .
- the total thickness of the solid electrolyte membrane / node catalyst layer electrode / forced sword catalyst layer electrode after hot pressing was about 1.5 mm.
- Comparative Example 1 when comparing the internal resistance value before and after long-term power generation, the internal resistance value of Comparative Example 1 (160 ⁇ ⁇ ) is that of Examples 1, 2, and 3 (95 ⁇ , 90 ⁇ , 92 ⁇ ). It was found that it was higher than ⁇ ). This is thought to be due to an increase in internal resistance due to a decrease in the adhesion strength of the electrodes due to changes over time in long-term power generation tests. Also, in the power maintenance rate, Comparative Example 1 is only 51%, while Example 1 has a high maintenance rate of 85%, Example 2 83%, and Example 3 82%. Indicated. From this, it was found that in each of Examples 1, 2, and 3, the battery characteristics were maintained even after long-term power generation.
- Example 4 is a multi-type membrane electrode assembly in which three rows of catalyst layer electrodes 12A having the shape shown in FIG. 2 are arranged in parallel, and Comparative Example 2 has three rows of catalyst layer electrodes 12 having the shape shown in FIG.
- This is a multi-type membrane electrode assembly connected in series.
- the length L1 of the long side 12b is 40 mm
- the length L2 of the short side 12a is 9 mm
- the chamfer size L3 of the missing corner of Example 4 is lmm
- the inter-electrode gap L5 is 1.5 mm
- the total width L6 was 30mm.
- the temperature was 125 in both Example 4 and Comparative Example 2.
- C. Hot pressing was performed under the conditions of 300 MPa / cm 2 pressure. Solid electrolyte membrane after hot pressing The total thickness of the Z anode catalyst layer electrode / forced sword catalyst layer electrode was about 1.5 mm.
- the pressed catalyst layer electrode is less likely to peel off the solid electrolyte membrane force, good battery performance can be stably obtained, and cellular phones, notebook computers, portable game machines can be obtained.
- a power source for mopile equipment such as
- the fuel cell of the present invention can maintain and restore the battery function by a simple operation. Therefore, the fuel cell of the present invention is extremely useful as a power source incorporated into a mobile device such as a mobile phone, a notebook computer, or a portable game machine. Is high.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Materials Engineering (AREA)
- Fuel Cell (AREA)
- Inert Electrodes (AREA)
Abstract
Description
Claims
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2007514743A JPWO2006118107A1 (ja) | 2005-04-27 | 2006-04-25 | 燃料電池および燃料電池用触媒層電極 |
EP06745674A EP1881548A4 (en) | 2005-04-27 | 2006-04-25 | FUEL CELL AND CATALYTIC LAYER ELECTRODE FOR FUEL CELL |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2005-129548 | 2005-04-27 | ||
JP2005129548 | 2005-04-27 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2006118107A1 true WO2006118107A1 (ja) | 2006-11-09 |
Family
ID=37307907
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2006/308646 WO2006118107A1 (ja) | 2005-04-27 | 2006-04-25 | 燃料電池および燃料電池用触媒層電極 |
Country Status (7)
Country | Link |
---|---|
US (1) | US20080096077A1 (ja) |
EP (1) | EP1881548A4 (ja) |
JP (1) | JPWO2006118107A1 (ja) |
KR (1) | KR20070114219A (ja) |
CN (1) | CN101176228A (ja) |
TW (1) | TW200707830A (ja) |
WO (1) | WO2006118107A1 (ja) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2009060604A1 (ja) * | 2007-11-07 | 2009-05-14 | Kabushiki Kaisha Toshiba | 燃料電池 |
JP2010218960A (ja) * | 2009-03-18 | 2010-09-30 | Aquafairy Kk | 燃料電池 |
JP2012182069A (ja) * | 2011-03-02 | 2012-09-20 | Ngk Spark Plug Co Ltd | 固体酸化物形燃料電池 |
WO2023277067A1 (ja) * | 2021-07-01 | 2023-01-05 | 日東電工株式会社 | 燃料電池、ギ酸塩の製造方法、及び発電方法 |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101534553B1 (ko) * | 2013-08-13 | 2015-07-10 | 주식회사 포스코 | 연료전지 |
EP3320576B1 (en) * | 2015-07-08 | 2021-11-17 | Agora Energy Technologies Ltd. | Redox flow battery with carbon dioxide based redox couple |
CN115284353A (zh) * | 2022-09-30 | 2022-11-04 | 江苏智泰新能源科技有限公司 | 一种软包锂离子电池弧形切边装置及其使用方法 |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06338335A (ja) * | 1993-05-27 | 1994-12-06 | Fuji Electric Co Ltd | 固体高分子電解質型燃料電池 |
JP2000123842A (ja) * | 1998-10-13 | 2000-04-28 | Matsushita Electric Ind Co Ltd | 燃料電池 |
JP2005108508A (ja) * | 2003-09-29 | 2005-04-21 | Toshiba Corp | アルコール型燃料電池用電極、アルコール型燃料電池用膜触媒層複合体及びアルコール型燃料電池。 |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1516311A (zh) * | 1998-06-16 | 2004-07-28 | ���µ�����ҵ��ʽ���� | 高分子电解质燃料电池 |
ATE539460T1 (de) * | 2000-09-01 | 2012-01-15 | Versa Power Systems Ltd | Elektrodenmuster für festoxidbrennstoffzellen |
-
2006
- 2006-04-25 EP EP06745674A patent/EP1881548A4/en not_active Withdrawn
- 2006-04-25 WO PCT/JP2006/308646 patent/WO2006118107A1/ja active Application Filing
- 2006-04-25 CN CNA2006800146045A patent/CN101176228A/zh active Pending
- 2006-04-25 JP JP2007514743A patent/JPWO2006118107A1/ja active Pending
- 2006-04-25 KR KR1020077024088A patent/KR20070114219A/ko not_active Application Discontinuation
- 2006-04-27 TW TW095115086A patent/TW200707830A/zh unknown
-
2007
- 2007-10-26 US US11/925,049 patent/US20080096077A1/en not_active Abandoned
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06338335A (ja) * | 1993-05-27 | 1994-12-06 | Fuji Electric Co Ltd | 固体高分子電解質型燃料電池 |
JP2000123842A (ja) * | 1998-10-13 | 2000-04-28 | Matsushita Electric Ind Co Ltd | 燃料電池 |
JP2005108508A (ja) * | 2003-09-29 | 2005-04-21 | Toshiba Corp | アルコール型燃料電池用電極、アルコール型燃料電池用膜触媒層複合体及びアルコール型燃料電池。 |
Non-Patent Citations (1)
Title |
---|
See also references of EP1881548A4 * |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2009060604A1 (ja) * | 2007-11-07 | 2009-05-14 | Kabushiki Kaisha Toshiba | 燃料電池 |
JP2010218960A (ja) * | 2009-03-18 | 2010-09-30 | Aquafairy Kk | 燃料電池 |
JP2012182069A (ja) * | 2011-03-02 | 2012-09-20 | Ngk Spark Plug Co Ltd | 固体酸化物形燃料電池 |
WO2023277067A1 (ja) * | 2021-07-01 | 2023-01-05 | 日東電工株式会社 | 燃料電池、ギ酸塩の製造方法、及び発電方法 |
Also Published As
Publication number | Publication date |
---|---|
US20080096077A1 (en) | 2008-04-24 |
TW200707830A (en) | 2007-02-16 |
KR20070114219A (ko) | 2007-11-29 |
JPWO2006118107A1 (ja) | 2008-12-18 |
EP1881548A1 (en) | 2008-01-23 |
CN101176228A (zh) | 2008-05-07 |
EP1881548A4 (en) | 2009-01-28 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR100821039B1 (ko) | 연료전지 스택 및 그 제조방법 | |
JP4420960B2 (ja) | 燃料電池および燃料電池層 | |
WO2006118107A1 (ja) | 燃料電池および燃料電池用触媒層電極 | |
JP2006331718A (ja) | 燃料電池 | |
TWI332726B (ja) | ||
TW201041215A (en) | Fuel cell | |
JP5062392B2 (ja) | 固体高分子型燃料電池 | |
JP2004079506A (ja) | 液体燃料電池 | |
JP5093640B2 (ja) | 固体電解質型燃料電池及びその製造方法 | |
WO2007034731A1 (ja) | 燃料電池 | |
US20210075048A1 (en) | Method for manufacturing membrane electrode assembly, and stack | |
JPWO2008050640A1 (ja) | 燃料電池 | |
JPWO2008023634A1 (ja) | 燃料電池 | |
JP5870643B2 (ja) | 固体高分子形燃料電池用膜電極接合体の製造方法 | |
JP4007883B2 (ja) | 液体燃料電池 | |
JP2008016258A (ja) | 燃料電池 | |
JP4236156B2 (ja) | 燃料電池 | |
JP2012074205A (ja) | 膜電極複合体およびアルカリ形燃料電池 | |
JP2004014148A (ja) | 液体燃料電池 | |
TW200836392A (en) | Fuel cell | |
JP2010170895A (ja) | 膜電極接合体の製造方法および製造装置 | |
JPWO2008062551A1 (ja) | 固体高分子型燃料電池 | |
WO2008023633A1 (fr) | Pile à combustible | |
KR101093708B1 (ko) | 연료전지용 전극 및 이를 포함하는 연료전지 | |
JP2013157227A (ja) | 直接アルコール型燃料電池 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
WWE | Wipo information: entry into national phase |
Ref document number: 200680014604.5 Country of ref document: CN |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
WWE | Wipo information: entry into national phase |
Ref document number: 2007514743 Country of ref document: JP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 1020077024088 Country of ref document: KR |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2006745674 Country of ref document: EP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 11925049 Country of ref document: US |
|
NENP | Non-entry into the national phase |
Ref country code: DE |
|
NENP | Non-entry into the national phase |
Ref country code: RU |
|
WWP | Wipo information: published in national office |
Ref document number: 2006745674 Country of ref document: EP |