WO2005020357A1 - 固体高分子型燃料電池 - Google Patents
固体高分子型燃料電池 Download PDFInfo
- Publication number
- WO2005020357A1 WO2005020357A1 PCT/JP2004/012333 JP2004012333W WO2005020357A1 WO 2005020357 A1 WO2005020357 A1 WO 2005020357A1 JP 2004012333 W JP2004012333 W JP 2004012333W WO 2005020357 A1 WO2005020357 A1 WO 2005020357A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- polymer electrolyte
- phosphate
- fuel cell
- membrane
- 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
- H01M4/90—Selection of catalytic material
- H01M4/9016—Oxides, hydroxides or oxygenated metallic salts
-
- 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
- H01M4/88—Processes of manufacture
- H01M4/8803—Supports for the deposition of the catalytic active composition
- H01M4/881—Electrolytic membranes
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/88—Processes of manufacture
- H01M4/8825—Methods for deposition of the catalytic active composition
- H01M4/8842—Coating using a catalyst salt precursor in solution followed by evaporation and reduction of the precursor
-
- 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
- H01M8/0289—Means for holding the electrolyte
-
- 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
- H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
- H01M8/1018—Polymeric electrolyte materials
- H01M8/102—Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer
- H01M8/1023—Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer having only carbon, e.g. polyarylenes, polystyrenes or polybutadiene-styrenes
-
- 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
- H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
- H01M8/1018—Polymeric electrolyte materials
- H01M8/1039—Polymeric electrolyte materials halogenated, e.g. sulfonated polyvinylidene fluorides
-
- 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
- H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
- H01M8/1018—Polymeric electrolyte materials
- H01M8/1041—Polymer electrolyte composites, mixtures or blends
- H01M8/1046—Mixtures of at least one polymer and at least one additive
- H01M8/1051—Non-ion-conducting additives, e.g. stabilisers, SiO2 or ZrO2
-
- 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
- H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
- H01M8/1018—Polymeric electrolyte materials
- H01M8/1069—Polymeric electrolyte materials characterised by the manufacturing processes
- H01M8/1086—After-treatment of the membrane other than by polymerisation
- H01M8/1088—Chemical modification, e.g. sulfonation
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
Definitions
- the present invention relates to a polymer electrolyte fuel cell, and more particularly, to a polymer electrolyte fuel cell suitable as an in-vehicle power source, a stationary small generator, a cogeneration system, and the like.
- a solid polymer electrolyte is a solid polymer material having an electrolyte group such as a sulfonic acid group in a polymer chain. Since solid polymer electrolytes have the property of firmly binding to specific ions and selectively transmitting cations or anions, they are formed into particles, fibers, or membranes, and are used for electrodialysis. It is used for various purposes such as diffusion analysis and battery diaphragm.
- the polymer electrolyte is formed into a membrane, and a membrane electrode assembly (MEA) in which electrodes are joined to both sides of the membrane.
- MEA membrane electrode assembly
- the electrode in a solid polymer fuel cell, the electrode generally has a two-layer structure of a diffusion layer and a catalyst layer.
- the diffusion layer is for supplying a reaction gas and electrons to the catalyst layer, and is made of carbon fiber, carbon paper, or the like.
- the catalyst layer is a reaction site of an electrode reaction, and is generally composed of a composite of a solid polymer electrolyte and carbon carrying a catalyst such as platinum.
- electrolyte membranes and electrolytes in catalyst layers used in electrochemical devices used under severe conditions include all-fluorinated electrolytes with excellent oxidation resistance (no C-H bond in the polymer chain.
- Electrolytes For example, Nafion (registered trademark, manufactured by Dupont), Aciplex (registered trademark, manufactured by Asahi Kasei Corporation), Flemion (registered trademark, manufactured by Asahi Glass Co., Ltd.) and the like. ) Is generally used.
- perfluorinated electrolytes have excellent oxidation resistance, but are generally very expensive. Therefore, in order to reduce the cost of various electrochemical devices using solid polymer electrolytes, hydrocarbon-based electrolytes (electrolytes containing C-H bonds in the polymer chain and no C-F bonds), or The use of partially fluorinated electrolytes (electrolytes containing both C-H and C-F bonds in the polymer chain) is also being considered.
- Japanese Patent Application Laid-Open No. 2001-118591 discloses that in order to suppress the decomposition of a hydrocarbon-based electrolyte due to peroxide radicals, peroxides (for example, , Hydrogen peroxide) is a highly durable solid polymer electrolyte in which transition metal oxides such as manganese oxide, ruthenium oxide, cobalt oxide, nickel oxide, chromium oxide, iridium oxide, and lead oxide are dispersed. Is disclosed.
- Japanese Patent Application Laid-Open No. 2000-106203 discloses a method for suppressing the degradation of a sulfonic acid resin composed of a copolymer of a fluorocarbon vinyl monomer and a hydrocarbon biermonomer due to hydrogen peroxide.
- a catalyst having an action of decomposing hydrogen peroxide on the sulfonic acid-based resin membrane wherein M n 0 2 , Ru 2 ,
- a solid polymer electrolyte membrane to which at least one of an oxide catalyst composed of Z ⁇ or the like, a macrocyclic metal complex catalyst composed of iron phthalocyanine, copper phthalocyanine, or the like, and a transition metal alloy catalyst composed of Cu—Ni or the like is disclosed. I have.
- Japanese Patent Application Laid-Open No. 2001-307752 discloses that in order to improve the durability of an aromatic polymer compound having a sulfonic acid group, a solution containing an aromatic polymer compound having a sulfonic acid group is required.
- Proton-conducting membrane obtained by adding tetraethoxysilane and phosphoric acid to an organic solvent and removing the solvent, in which a polymer compound, a silicon oxide, and an inorganic compound mainly composed of a phosphoric acid derivative are compounded. Is disclosed.
- Japanese Patent Application Laid-Open No. 2001-213987 discloses that in order to maintain high proton conductivity under high temperature conditions of 100 ° C or higher, graft polymerization of polyvinyl pyridine onto an ethylene-tetrafluoroethylene copolymer membrane is carried out.
- a high-temperature proton-conductive electrolyte membrane further doped with phosphoric acid has been disclosed.
- Japanese Patent Application Laid-Open No. 06-103983 does not consider oxidation resistance at all.
- a perfluoroca one Pons sulfonic acid membrane, zirconium phosphate compound (Z r (0 3 P CH 2 S0 3 H) 2) or solid polymer electrolyte membrane type using a material obtained by adding phosphoric acid (H 3 P0 4) as an electrolyte membrane A fuel cell is disclosed.
- Noble metals such as Pt, Ru, Ir and Rh or oxides thereof have an action of decomposing peroxides. Therefore, when these powders are added to a hydrocarbon-based electrolyte or a partially fluorine-based electrolyte, the generation of peroxide radicals is suppressed, and the oxidation resistance is improved. However, since these noble metals have low resources and are expensive, it is not practical to add the noble metal or its oxide.
- transition metal oxides such as manganese dioxide, separate peroxides. It has the effect of dissolving and is less expensive than precious metals or their oxides.
- conventionally known transition metal oxides do not always have sufficient decomposition activity for peroxides. In particular, if this is applied to applications requiring high oxidation resistance, such as a polymer electrolyte fuel cell, sufficient durability cannot be obtained.
- the inorganic compound obtained by reacting tetraethoxysilane with phosphoric acid described in Japanese Patent Application Laid-Open No. 2001-3077752 is synthesized at a relatively low temperature.
- the structure tends to be unstable. Therefore, in an environment in which water is in contact with high temperature or low pH water, the inorganic compound gradually elutes, and the oxidation resistance decreases with time.
- perfluorinated electrolytes have conventionally been considered to have high resistance to peroxide radicals and not degrade even when used for a long time in an environment where peroxide radicals coexist.
- the present inventors have found that even a perfluorinated electrolyte deteriorates over time when used for a long time under the operating conditions of a fuel cell. Therefore, for applications requiring a high level of oxidation resistance, it is desired to further improve the durability of the electrolyte.
- the problem to be solved by the present invention is to improve the oxidation resistance of an electrolyte membrane and its durability by a low-cost method, thereby improving the durability of a polymer electrolyte fuel cell. is there.
- the present invention Another issue is that the oxidation resistance of perfluorinated electrolytes and their durability are improved by low-cost methods, thereby further improving the durability of solid polymer fuel cells using perfluorinated electrolytes. To make it happen. Disclosure of the invention
- the present invention provides a solid polymer electrolyte fuel cell including a membrane electrode assembly in which electrodes are joined to both surfaces of a solid polymer electrolyte membrane, wherein the solid polymer electrolyte membrane and the electrode
- the gist is that a phosphate containing a rare earth element and at least one metal element selected from Ti, Fe, A1 and Bi is fixed to at least one of them.
- a phosphate containing a predetermined metal element is fixed to at least one of the polymer electrolyte membrane and the electrode, radicalization of peroxide, and This suppresses radical decomposition of the organic polymer.
- the phosphate containing the predetermined metal element has relatively low solubility in water at high temperature or low pH, excellent oxidation resistance can be maintained for a long period of time.
- the deterioration of the perfluorinated electrolyte due to peroxide radicals is suppressed. Therefore, if this is applied to a polymer electrolyte fuel cell, the durability of the polymer electrolyte fuel cell is further improved.
- Figure 1 is an X-ray diffraction profile of the C e (N 0 3) 3 H 3 P 0 4 white powder that obtained aqueous solution was added to the aqueous solution.
- the polymer electrolyte fuel cell according to the present invention, electrodes are bonded to both surfaces of the polymer electrolyte membrane.
- Membrane electrode assembly MEA
- the polymer electrolyte fuel cell usually has a structure in which both sides of such a MEA are sandwiched between separators having gas flow paths, and a plurality of these are stacked.
- the material of the solid polymer electrolyte membrane is not particularly limited, and various materials can be used.
- the material of the solid polymer electrolyte membrane is a hydrocarbon-based electrolyte containing a C-H bond in the polymer chain and no C-F bond, and a C-F bond in the polymer chain.
- Any of the fluorine-containing electrolytes may be used.
- the fluorine-based electrolyte may be a partial fluorine-based electrolyte containing both a C—H bond and a C—F bond in a polymer chain, or a C—F bond in a polymer chain, and It may be a perfluorinated electrolyte containing no C—H bond.
- the molecular structure of the polymer constituting the solid polymer electrolyte membrane is not particularly limited, and may be linear or branched, or may have a cyclic structure.
- the type of the electrolyte group provided in the solid polymer electrolyte is not particularly limited.
- Preferred examples of the electrolyte group include a sulfonic acid group, a carboxylic acid group, a phosphonic acid group, and a sulfonimide group.
- the solid polymer electrolyte may include only one of these electrolyte groups, or may include two or more of these electrolyte groups. Further, these electrolyte groups may be directly bonded to the linear solid polymer compound, or may be bonded to either the main chain or the side chain of the branched solid polymer compound. good.
- hydrocarbon-based electrolytes include polyamides, polyacetals, and polyacetals in which an electrolyte group such as a sulfonic acid group is introduced into one of the polymer chains.
- polystyrene a polystyrene-graft-ethylenetetrafluoroethylene copolymer
- an electrolyte group such as a sulfonic acid group is introduced into one of the polymer chains.
- PS—g—ETFE polystyrene-graft-polytetrafluoroethylene, and the like, and derivatives thereof.
- perfluorinated electrolyte examples include Nafion (registered trademark) manufactured by DuPont, Aciplex (registered trademark) manufactured by Asahi Kasei Corporation, Flemion (registered trademark) manufactured by Asahi Glass Co., Ltd., and the like. Derivatives are mentioned as a preferred example.
- the solid polymer electrolyte membrane constituting the MEA is obtained by impregnating various solid polymer electrolytes or an electrolyte solution such as phosphoric acid into pores of a reinforcing material made of a porous polymer compound. May be a complex o
- fluorine-based electrolytes especially perfluorinated electrolytes, are polymers Since it has a C_F bond in the chain and has excellent oxidation resistance, if the present invention is applied to this, a polymer electrolyte fuel cell having excellent oxidation resistance and durability can be obtained. Is obtained.
- the electrode that constitutes the MEA usually has a two-layer structure of a catalyst layer and a diffusion layer, but may be composed of only the catalyst layer.
- the electrode When the electrode has a two-layer structure of a catalyst layer and a diffusion layer, the electrode is bonded to the electrolyte membrane via the catalyst layer.
- the catalyst layer is a part to be a reaction field of an electrode reaction, and includes a catalyst or a carrier supporting the catalyst, and an electrolyte in the catalyst layer covering the periphery thereof.
- the most suitable catalyst is used in accordance with the purpose of use of the MEA and the conditions of use.
- platinum In the case of a polymer electrolyte fuel cell, platinum, a platinum alloy, palladium, ruthenium, rhodium, or the like, or an alloy thereof is used as a catalyst.
- the optimal amount of the catalyst contained in the catalyst layer is selected according to the application of the MEA, the use conditions, and the like.
- the catalyst carrier is for carrying fine particles of the catalyst and for transferring electrons in the catalyst layer.
- the catalyst carrier graphite, acetylene black, oil furnace black, activated carbon, fullerene, carbon nanophone, carbon nanotube, VGCF (vapor-grown carbon fiber), and the like are generally used.
- the optimal amount of the catalyst carried on the surface of the catalyst carrier is selected according to the materials of the catalyst and the catalyst carrier, the application of the MEA, the conditions of use, and the like.
- the electrolyte in the catalyst layer is for transferring protons between the solid polymer electrolyte membrane and the electrode.
- the electrolyte in the catalyst layer the same material as that of the solid polymer electrolyte membrane is usually used, but a different material may be used.
- the optimal amount of the electrolyte in the catalyst layer is selected according to the use of the MEA, the use conditions, and the like.
- the diffusion layer transfers electrons to and from the catalyst layer and simultaneously supplies the reaction gas to the catalyst layer.
- carbon paper, carbon cloth, or the like is used for the diffusion layer.
- the surface of carbon paper or the like coated with a mixture of a powder of a water-repellent polymer such as polytetrafluoroethylene and a powder of carbon may be used as the diffusion layer.
- the polymer electrolyte fuel cell according to the present invention is characterized in that a phosphate containing a predetermined metal element is fixed on at least one of the solid polymer electrolyte membrane and the electrode constituting the MEA.
- the metal element contained in the phosphate comprises a rare earth element and at least one element selected from Ti, Fe, A1 and Bi.
- the rare earth elements refer to Sc of atomic number 21 and Y of atomic number 39, and lanthanide elements from La of atomic number 57 to Lu of atomic number 71.
- Each of these phosphates has a function of decomposing peroxide, is stable even at a relatively high temperature and / or a low pH, and is hardly eluted.
- Ce, Y, Ti, Fe, Al, and Bi are relatively rich in resources and inexpensive compared to noble metals, so MEA and polymer electrolyte fuel cells using the same are used. Cost can be reduced.
- phosphates of rare earth elements, especially phosphates containing Ce have a high peroxide decomposition activity, so that the durability of MEA and polymer electrolyte fuel cells using the same are dramatically improved. It can be done.
- the phosphate orthophosphoric acid (H 3 P 0 4), main Yuri phosphate (HP0 3), diphosphate (pyrophosphate, H 4 P 2 0 7) , triphosphoric acid (H Various phosphoric acid salts such as 5 P 3 O 10 ) having relatively low solubility in high-temperature and / or low-pH water.
- the phosphate is at least room temperature (20 ⁇ 2 5 ° C) in the solubility product K sp (RT) is virtuous preferable not more 10 8 or less .
- the solubility product K sp (T) at the actual use temperature (80 to 100 ° C) of the polymer electrolyte fuel cell is generally the solubility product K s at room temperature. (RT) Although it is one or two orders of magnitude larger, practically sufficient durability can be obtained if the solubility product K sp (RT) is at least the above value.
- Definitive room temperature phosphate solubility product K sp (RT) is preferably not more than 10- 1 Q, preferably in the et, or less 10_ 2G.
- the phosphate may include only one of the above-described metal elements, or may include two or more metal elements.
- other elements that do not adversely affect peroxide decomposition and / or phosphate solubility eg, Ca, Sr, etc.
- the phosphates may be affected by some anions (eg, F-, OH, etc.) in which some of the phosphate ions do not adversely affect peroxide decomposition and / or salt solubility. It may be replaced.
- the tertiary salt of orthophosphoric acid or its hydrate represented by the following formula (1) has a high peroxide decomposing action and poor solubility, and thus MEA It is particularly suitable as a phosphate to be added.
- the rare earth elements, and, T i, Fe at least selected from A 1 and B earth one metal element.
- M 2 do not adversely affect the decomposition and Z or sparingly soluble peroxide element (e.g., Ca, etc. S r.)
- P 0 4 , F, OH is orthophosphate ions (P 0 4 3 -). that some of it may be substituted by F- or OH Shown.)
- the phosphate may be fixed to any of the electrolyte membrane, the catalyst layer, and the diffusion layer that constitute the MEA. Further, when the phosphate is fixed to the electrolyte membrane, the catalyst layer and / or the diffusion layer, the fixing place is not particularly limited.
- the phosphate when phosphate is immobilized on the electrolyte membrane, the phosphate may be immobilized on the membrane surface, or may be uniformly immobilized inside the membrane. good.
- the phosphate when the phosphate is fixed to the catalyst layer, the phosphate may be fixed to the surface of the catalyst or the carrier supporting the catalyst and / or the electrolyte in the catalyst layer. Alternatively, it may be fixed inside the electrolyte in the catalyst layer.
- the phosphate when the phosphate is fixed to the diffusion layer, the phosphate may be uniformly fixed to the entire diffusion layer, or may be fixed to the surface of the diffusion layer on the catalyst layer side or on the separation surface. May be.
- peroxide is generally generated by a side reaction of an electrode reaction, and the generated peroxide is diffused to various parts together with water in the fuel cell. Therefore, it is preferable that the phosphate is fixed in the vicinity of the electrode which is the source of the peroxide.
- the optimal amount of phosphate fixed to the polymer electrolyte membrane, catalyst layer and / or diffusion layer is selected according to the application and required characteristics of the MEA and the polymer electrolyte fuel cell using it. I do. In general, as the amount of the phosphate fixed becomes larger, a polymer electrolyte fuel cell having more excellent oxidation resistance and durability can be obtained.
- peroxide such as hydrogen peroxide is generated as a side reaction of the electrode reaction.
- This peroxide forms a transition metal ion (M n + / M ( n + 1 ) +) whose valence changes, such as Fe 2 + Fe 3 + ion.
- radical decomposition occurs by the oxidation reaction of the following formula (2) or the reduction reaction of the following formula (3).
- the electrolyte membrane is generally humidified using auxiliary equipment, and there is a transition metal ion derived from piping and the like near MEA.
- peroxide radicals are generated in the environment.
- peroxide radicals (HOO, HO, etc.) generated by radical decomposition of peroxide break the C—H bond of the organic polymer compound, leading to deterioration and lower molecular weight of the organic polymer compound. It is known. Therefore, if a conventional hydrocarbon-based electrolyte or partial fluorine-based electrolyte is used as it is in a polymer electrolyte fuel cell, sufficient durability for practical use cannot be obtained.
- perfluorinated electrolytes were not considered to be deteriorated by peroxide radicals because they do not contain C—H bonds in their polymer chains.
- the present inventors have found that even with a perfluorinated electrolyte, it deteriorates under the operating environment of the fuel cell, and that the F ions are discharged from the fuel cell due to the deterioration, and that the causative substance is a peroxide. It is found to be a radical.
- a phosphate of a predetermined metal element such as a rare earth element has an action of suppressing deterioration due to peroxide radicals. This is because on the solid surface of a phosphate such as a rare earth element, before the peroxide is radically decomposed, the reduction reaction of the following formula (4) or the oxidation reaction of the following formula (5) causes the ionization. It is considered to be disassembled.
- reaction on the solid surface is eventually decomposed into water and oxygen by collision of two molecules of hydrogen peroxide as shown in the following equation (6) from equations (4) and (5). It is expressed as a catalytic cracking reaction.
- a phosphate such as a rare earth element is fixed to at least one of the solid polymer electrolyte membrane, the catalyst layer, and the diffusion layer, generation of peroxide radicals is suppressed, and as a result, Deterioration of organic compounds, reduction of molecular weight, etc. are suppressed. Further, even when a hydrocarbon-based electrolyte membrane or a partially fluorine-based electrolyte membrane is used as the solid polymer electrolyte membrane, a polymer electrolyte fuel cell exhibiting high durability can be obtained.
- phosphates such as rare earth elements have relatively low solubility in high-temperature or low-pH water, even if they are used for a long time in a fuel cell environment, phosphates are less likely to be eluted. Therefore, if this is fixed to any part of the MEA, a polymer electrolyte fuel cell exhibiting high durability over a long period of time can be obtained. Further, phosphates of rare earth elements and the like have low solubility in phosphoric acid, and therefore, even when the present invention is applied to a polymer electrolyte fuel cell using phosphoric acid as an electrolyte, the long term A polymer electrolyte fuel cell exhibiting high durability over the whole is obtained.
- the F ion elution rate in the immersion test described later is 5 (/ g). / cmV r) or less, and an all-fluorinated electrolyte in which the F ion concentration does not increase even when the immersion test is repeated is obtained.
- the F ion elution rate in the immersion test is 1 (g / cm 2 / hr) or less, and the F ion concentration does not increase even if the immersion test is repeated A perfluorinated electrolyte is obtained.
- phosphates that have a decomposing effect on peroxide and are hardly soluble, phosphates of Ce, Y, Fe, Ti, Bi or A1 are relatively rich in resources. It is cheaper than precious metals such as Pt and Pt. Therefore, if these phosphates are used, the durability of the polymer electrolyte fuel cell can be improved without increasing the cost.
- Ce phosphate is relatively inexpensive and has a high peroxide decomposing effect, so it does not increase the cost of the polymer electrolyte fuel cell and has a high durability. Can be dramatically improved.
- the rare earth elements such as La and Nd are converted into so-called phosphates derived from mischmetals containing Ce, so that the rare earth elements can be separated from inexpensive raw materials without being separated from each other. It is also possible to produce e-containing phosphates.
- the first method is a method of fixing phosphate to a solid polymer electrolyte membrane, a catalyst layer and / or a diffusion layer using solid phosphate powder as a starting material.
- the particle size of the phosphate is preferably 0.05 m or more. If the particle size of the phosphate is less than 0.05 m, the specific surface area increases, so that the solubility of the phosphate increases and the long-term stability is poor. On the other hand, if the particle size of the phosphate exceeds 5 m, it becomes difficult to uniformly disperse the phosphate on or in the solid polymer electrolyte membrane, the catalyst layer and / or the diffusion layer.
- the membrane is formed by a casting method from a solution containing the solid polymer electrolyte dissolved in a suitable solvent or melted by heat.
- a predetermined amount of phosphate powder may be dispersed in a solution containing the solid polymer electrolyte.
- a phosphate powder may be sprayed on the surface, or a solution in which the phosphate powder is dispersed may be applied.
- a solution containing a catalyst or a carrier supporting the catalyst and a solid polymer electrolyte hereinafter referred to as “catalyst ink”.
- phosphate powder is further dispersed, and a catalyst ink containing the phosphate powder is sprayed or doctor bladed onto an electrolyte membrane, diffusion layer, tetrafluoroethylene sheet, or the like. What is necessary is just to apply to the surface of a suitable base material.
- phosphate When phosphate is fixed on the surface of the catalyst layer, specifically, after forming the catalyst layer using a catalyst ink containing no phosphate powder on the surface of the electrolyte membrane, the diffusion layer, or the base material, A phosphate powder may be sprayed on the surface of the catalyst layer, or a solution in which the phosphate powder is dispersed may be applied.
- phosphate powder when phosphate is fixed on the surface of the diffusion layer, phosphate powder may be sprayed on the surface of the diffusion layer, or a solution in which the phosphate powder is dispersed may be applied.
- a phosphate powder When a water-repellent layer is formed on the surface of the diffusion layer, a phosphate powder is further added to a mixture of a water-repellent agent such as polytetrafluoroethylene and carbon, and this is added to the diffusion layer. It may be applied to the surface.
- the second method is a solid polymer electrolyte membrane or a precursor thereof, a catalyst layer, or a diffusion layer, or a solid polymer electrolyte membrane having a catalyst layer formed on its surface or a precursor, a diffusion layer, or A substrate such as tetrafluoroethylene sheet is brought into contact with either a first solution containing a water-soluble salt or an organometallic complex containing a metal element such as a rare earth element, or a second solution containing phosphoric acid. And then contacting the other.
- the second method is particularly suitable as a phosphate fixing method because the phosphate can be more uniformly fixed at a desired position.
- the salt used in the second method only needs to be water-soluble, and its type is not particularly limited.
- the water-soluble salt specifically, rare earths
- Preferable examples include acetates, oxalates, nitrates, sulfates, and chlorides of metal elements such as elements.
- the organometallic complex may be liquid at room temperature or soluble in an appropriate solvent.
- Specific examples of the organometallic complex include tert-butoxide ((CH 3 ) 3 CO—) of a metal element such as a rare earth element, ethylhexanoneate, octane dionate, and isopropoxide ((CH 3 ) 2 CHO-) and the like are mentioned as a preferable example.
- phosphate is uniformly dispersed in a solid polymer electrolyte membrane or a precursor thereof (for example, a sulfonyl fluoride form of Naphion (registered trademark) (hereinafter, simply referred to as “F form”)).
- F form a sulfonyl fluoride form of Naphion (registered trademark)
- the solid polymer electrolyte membrane or its precursor is immersed for a predetermined time in a first solution containing a water-soluble salt or organometallic complex, and the water-soluble salt or organometallic complex is added. Adsorb or ion exchange.
- the solid polymer electrolyte membrane or a precursor thereof is immersed in the second solution to adsorb phosphoric acid or ion-exchange with phosphoric acid, and then immersed in the first solution.
- it may be washed with ion-exchanged water.
- first solution and the second solution may be applied, and then the other may be applied or immersed in the other, and then washed with ion-exchanged water.
- the solid polymer electrolyte membrane, the diffusion layer or the base material on which the catalyst layer is formed is immersed in either the first solution or the second solution, Next, it may be immersed in the other, and further washed with ion exchanged water. Further, one of the first solution and the second solution is applied to the surface of the solid polymer electrolyte membrane, the diffusion layer or the catalyst layer formed on the surface of the substrate, and then the other is applied or immersed in the other. Further, it may be washed with ion-exchanged water.
- the diffusion layer should be immersed in one of the first solution and the second solution, then immersed in the other, and further washed with ion-exchanged water. Good.
- phosphate is immobilized on the surface of the diffusion layer, one of the first solution and the second solution is applied to the surface of the diffusion layer, and then the other is applied or immersed in the other. It is good to wash with.
- washing with ion-exchanged water may be omitted.
- the first solution may be used as it is, in order to stabilize the water-soluble salts or organometallic complexes, complexing agents such Beautique phosphate optionally (C 6 H 8 0 7) May be added.
- the catalyst layers are formed on both sides of the solid polymer electrolyte membrane according to a conventional method. If the diffusion layers are joined in this order, and if necessary, a MEA in which phosphate is fixed at a predetermined site can be obtained. Furthermore, the polymer electrolyte fuel cell according to the present invention can be obtained by sandwiching both sides of the MEA with a separator provided with a gas flow path and stacking a predetermined number of them.
- the polymer electrolyte fuel cell obtained in this way is one of MEA Since phosphates such as rare earth elements are fixed to the part, high resistance to peroxide radicals is exhibited. Further, phosphates such as rare earth elements are stable to high temperature and / or low pH water, so they are not eluted and can maintain high durability for a long period of time.
- the phosphate when the second method is used as the phosphate fixing method, the phosphate can be uniformly fixed to a target portion of the solid polymer electrolyte membrane, the catalyst layer and / or the diffusion layer. Therefore, a relatively small amount of phosphate can provide a high peroxide decomposing action, and a solid polymer fuel cell with excellent durability can be obtained.
- Ce ion concentration 0. 05wt%.
- a perfluorinated electrolyte membrane Naphion (registered trademark) membrane
- Hitatsubushi a membrane 0. 1M H 3 P 0 4 aqueous 1 ⁇ 0 m 1 was hydrolyzed in 90 ° Cx 1 hr.
- the membrane gradually became white and Ce phosphate was fixed in the membrane. Further, after washing several times the membrane with deionized water, heated 90 ° Cx 30 minutes with deionized water to remove excess H 3 P 0 4.
- the fixed amount of Ce phosphate determined from the change in membrane weight was 1.6 wt%.
- this membrane was placed in 200 ml of an aqueous solution containing 1 wt% of hydrogen peroxide and ferrous chloride (FeCl 2 ) corresponding to 14 ppm of Fe, and immersion test was performed at 100 ° CX24. Was done. After the immersion test, the concentration of F ions eluted in the aqueous solution was measured with an ion selective electrode manufactured by Orion. As a result, the F ion concentration was 0.80 ppm. The decrease in membrane weight before and after the immersion test was -0.3 wt%.
- FeCl 2 ferrous chloride
- Example 2 As a water-soluble salt, except for using nitric acid Gadoriniumu (Gd (N0 3) 3) , according to the same procedure as in Example 1, a perfluorinated electrolyte membrane having Gd phosphate fixed thereon was produced. The fixed amount of Gd phosphate determined from the change in membrane weight was 4.3 wt%. The obtained membrane was measured for F ion concentration and membrane weight loss under the same conditions as in Example 1. As a result, the F ion concentration was 18.4 ppm, and the decrease in film weight was -1.3 wt%.
- Gd (N0 3) 3 nitric acid Gadoriniumu
- Example 2 As a water-soluble salt, except for using nitric acid Lee Ttoriumu (Y (N0 3) 3) , the same steps as in Example 1 to prepare a wholly fluorinated electrolyte Shitsumaku which Y phosphate is fixed. The fixed amount of Y phosphate determined from the change in membrane weight was 6.8 wt%. The F ion concentration of the obtained membrane was measured under the same conditions as in Example 1. As a result, the F ion concentration was 18.8 ppm.
- Example 6 To water 100 ml, except for dissolved sulfate titanium as T i ion concentration of 3 Owt% (T i 2 ( S0 4) 3) in accordance with the same procedures as in Example 1, T A perfluorinated electrolyte membrane to which i-phosphate was fixed was prepared. The fixed amount of Ti phosphate determined from the change in membrane weight was 0.3 wt%. For the obtained membrane, the F ion concentration and the weight loss of the membrane were measured under the same conditions as in Example 1. As a result, the F ion concentration was 15.0 ppm, and the weight loss of the membrane was -1.3 wt%.
- Example 2 As a water-soluble salt, except for using aluminum nitrate (A1 (N0 3) 3) , the same steps as in Example 1 to prepare a wholly fluorinated electrolyte membranes which A 1 phosphate is fixed.
- the fixed amount of A 1 phosphate determined from the change in membrane weight was 0.4 wt%.
- the F ion concentration and the weight loss of the membrane were measured under the same conditions as in Example 1. As a result, the F ion concentration was 17.4 ppm, and the decrease in membrane weight was 2.8 wt%.
- Example 1 Using the perfluorinated electrolyte membrane used in Example 1 as it was (no treatment), the F ion concentration and the decrease in membrane weight were measured under the same conditions as in Example 1. As a result, the F ion concentration was 45.3 ppm, and the decrease in membrane weight was -6.7 wt%.
- Table 1 shows the results obtained in Examples 1 to 7 and Comparative Examples 1 and 2.
- Example 2 In accordance with the same procedure as in Example 1, a perfluorinated electrolyte membrane having Ce phosphate immobilized thereon was produced. Next, the immersion test was repeated twice under the same conditions as in Example 1, and the first and second F ion concentrations were measured. Furthermore, the F ion elution rate was calculated from the measured F ion concentration. As a result, the first F ion elution rate was 0.13 ( ⁇ g / cm 2 / hr), while the second F ion elution rate was 0.04 (g / cmVhr). However, even when the immersion test was repeated twice, it was found that the F-ion elution inhibitory action was maintained.
- the decrease in film weight after the first immersion test was -0.3 wt%, compared to the initial state after the second immersion test (before the first immersion test).
- the weight loss of the film was 0.3 wt%, and almost no weight loss occurred during the second immersion test.
- Example 3 a perfluorinated electrolyte membrane to which La phosphate was fixed was produced.
- the immersion test was repeated twice under the same conditions as in Example 1, and the first and second F ion elution rates were calculated.
- the first F ion elution rate was 0.94 (g / cm 2 / hr)
- the second F ion elution rate was 0.72 ( ⁇ g / cm 2 Zhr).
- B i phosphate was prepared wholly fluorinated electrolyte Shitsumaku fixed .
- the fixed amount of Bi phosphate determined from the change in membrane weight was 18 wt%.
- the immersion test was repeated twice under the same conditions as in Example 1, and the first and second F ion elution rates were calculated.
- the first F ion elution rate was 3.20 ( ⁇ g / cm 2 Zhr)
- the second F ion elution rate was 2.25 (zg / cmV r).
- the F ion elution rate decreased compared to the first time.
- the film weight loss after the first immersion test was -1 lwt%, while the film weight loss from the initial state after the second immersion test was 1. 3. Owt%, In the immersion test, the film weight was further reduced. This is probably because zirconium phosphate eluted from the film due to the relatively high solubility of zirconium phosphate.
- the immersion test was repeated twice under the same conditions as in Example 1 using the perfluorinated electrolyte membrane used in Example 1 as it was (no treatment), and the first and second F ion elution rates were calculated.
- the first F ion elution rate was 7.18 (/ g / cms / hr)
- the second F ion elution rate was 6.32 (g / cm 2 / hr).
- the decrease in film weight after the first immersion test was -6.7 wt%
- the decrease in film weight from the initial state after the second immersion test was -10.6 wt%. In the immersion test, the film weight was further reduced.
- Table 2 shows the results obtained in Examples 8 to 10 and Comparative Examples 3 and 4.
- ⁇ indicates that the F ion elution rate did not increase for the second time
- ⁇ indicates that the F ion elution rate increased or the F ion elution rate was 5 ( ⁇ g / cm 2 / r). Those that exceeded were judged as "X”.
- Example 8 Ge phosphate 0.13 0.04 -0.3 -0.3 O
- Example 9 La phosphate 0.94 0.72 1-o
- Example 10 Bi phosphate 3.20 2.25 1 o
- Comparative example 3 Zr phosphate 1.19 4.93 -1.1- 3.0 X
- Comparative Example 4 1 7.18 6.32 -6.7 -10.6 X
- PtZC catalyst 0.5 g, cerium phosphate (CePO 4 ) powder (average particle size 2 ⁇ m, purity 99.9%, manufactured by Kojundo Chemical Laboratory Co., Ltd.) 0.5 wt% equivalent, distilled water 2.0 g, ethanol 2.5 g propylene glycol 1.0 g, 22 wt% Naphion (registered trademark) solution (manufactured by DuPont) 0.9 g, added in this order,
- the catalyst ink was prepared by dispersing with a sonic homogenizer. This was applied onto a tetrafluoroethylene sheet and dried to obtain a force sword transfer electrode. Pt amount was constant in the range of 0. 5 ⁇ 0. 6 mgZc m 2.
- Electrodes were cut into 36 mm squares and thermocompressed (120 ° C; 5 Okgf / cm 2 (4.9 MPa)) to one side of a perfluorinated electrolyte membrane (Naphion (registered trademark) membrane) to form MEA. Produced.
- MEA was manufactured according to the same procedure as in Example 11 except that the perfluorinated electrolyte membrane used in Example 1 was used as it was (no treatment).
- the F ion elution rate was 4.01 (/ g / cm 2 / r).
- the F ion elution rate was 0 03 (/ g / cm 2 / hr) ⁇ and 0.02 ( ⁇ g / cm 2 / hr). It was understood that it was suppressed to.
- the polymer electrolyte fuel cell according to the present invention can be applied to an in-vehicle power source, a stationary small generator, a cogeneration system, and the like.
- the use of the solid polymer electrolyte in which the phosphate containing the predetermined metal element is fixed is not limited to the electrolyte membrane or the electrolyte in the catalyst layer of the polymer electrolyte fuel cell, and is not limited to the water electrolysis device, the halogen, and the like. It can also be used as an electrolyte membrane and electrode material for various electrochemical devices such as hydrofluoric acid electrolyzer, salt electrolyzer, oxygen and Z or hydrogen concentrator, humidity sensor and gas sensor.
Landscapes
- Chemical & Material Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Manufacturing & Machinery (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Materials Engineering (AREA)
- Composite Materials (AREA)
- Crystallography & Structural Chemistry (AREA)
- Fuel Cell (AREA)
Abstract
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA002534431A CA2534431A1 (en) | 2003-08-22 | 2004-08-20 | Polymer electrolyte fuel cell |
EP04772289A EP1662595A4 (en) | 2003-08-22 | 2004-08-20 | ELECTROCHEMICAL CELL WITH SOLID POLYMER |
US11/356,264 US20060199063A1 (en) | 2003-08-22 | 2006-02-17 | Polymer electrolyte fuel cell |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2003299067A JP4979179B2 (ja) | 2003-08-22 | 2003-08-22 | 固体高分子型燃料電池およびその製造方法 |
JP2003-299067 | 2003-08-22 |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US11/356,264 Continuation US20060199063A1 (en) | 2003-08-22 | 2006-02-17 | Polymer electrolyte fuel cell |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2005020357A1 true WO2005020357A1 (ja) | 2005-03-03 |
Family
ID=34213742
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2004/012333 WO2005020357A1 (ja) | 2003-08-22 | 2004-08-20 | 固体高分子型燃料電池 |
Country Status (6)
Country | Link |
---|---|
US (1) | US20060199063A1 (ja) |
EP (1) | EP1662595A4 (ja) |
JP (1) | JP4979179B2 (ja) |
CN (1) | CN100413135C (ja) |
CA (1) | CA2534431A1 (ja) |
WO (1) | WO2005020357A1 (ja) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1729361A3 (en) * | 2005-06-02 | 2008-01-09 | Mitsubishi Heavy Industries, Ltd. | Solid polyelectrolyte fuel cell |
EP1946400A2 (en) * | 2005-10-28 | 2008-07-23 | 3M Innovative Properties Company | High durability fuel cell components with cerium oxide additives |
EP1970984A1 (en) * | 2005-12-28 | 2008-09-17 | Toyota Jidosha Kabushiki Kaisha | Catalyst for fuel cell electrode, process for producing catalyst for fuel cell electrode, film-electrode assembly, and fuel cell |
US7879475B2 (en) | 2005-05-31 | 2011-02-01 | Kabushiki Kaisha Toyota Chuo Kenkyusho | Solid polymer electrolyte, solid polymer fuel cell and method for manufacturing the fuel cell |
US7943249B2 (en) | 2004-06-22 | 2011-05-17 | Asahi Glass Company, Limited | Liquid composition, process for its production and process for producing membrane-electrode assembly for polymer electrolyte fuel cells |
US8962215B2 (en) | 2004-06-22 | 2015-02-24 | Asahi Glass Company, Limited | Electrolyte membrane for polymer electrolyte fuel cell, process for its production and membrane-electrode assembly for polymer electrolyte fuel cell |
US9512033B2 (en) | 2012-01-23 | 2016-12-06 | Sumitomo Electric Industries, Ltd. | Optical fiber preform |
Families Citing this family (43)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP5286651B2 (ja) * | 2004-06-22 | 2013-09-11 | 旭硝子株式会社 | 液状組成物、その製造方法及び固体高分子形燃料電池用膜電極接合体の製造方法 |
KR100970358B1 (ko) * | 2004-06-22 | 2010-07-15 | 아사히 가라스 가부시키가이샤 | 액상 조성물, 그 제조 방법 및 고체 고분자형 연료 전지용막 전극 접합체의 제조 방법 |
CN1981400B (zh) * | 2004-07-12 | 2012-04-04 | 旭硝子株式会社 | 固体高分子型燃料电池用电解质膜、其制造方法以及固体高分子型燃料电池用膜电极接合体 |
JP2006099999A (ja) * | 2004-09-28 | 2006-04-13 | Asahi Glass Co Ltd | 固体高分子形燃料電池用電解質膜、その製造方法及び固体高分子形燃料電池用膜電極接合体 |
JP5247974B2 (ja) * | 2004-10-05 | 2013-07-24 | 旭硝子株式会社 | 固体高分子形水素・酸素燃料電池用電解質膜の製造方法 |
JP4821147B2 (ja) * | 2005-03-18 | 2011-11-24 | トヨタ自動車株式会社 | 燃料電池及び燃料電池システム |
JP2006294293A (ja) * | 2005-04-06 | 2006-10-26 | Toyota Motor Corp | 燃料電池 |
JP4810868B2 (ja) * | 2005-04-19 | 2011-11-09 | 旭硝子株式会社 | 固体高分子型燃料電池用電解質膜、その製造方法、固体高分子型燃料電池用膜電極接合体及びその運転方法 |
JP2006318755A (ja) * | 2005-05-12 | 2006-11-24 | Asahi Glass Co Ltd | 固体高分子形燃料電池用膜電極接合体 |
JP4765401B2 (ja) * | 2005-05-18 | 2011-09-07 | 旭硝子株式会社 | 固体高分子形燃料電池用膜の製造方法及び固体高分子形燃料電池用膜電極接合体の製造方法 |
JP4517398B2 (ja) * | 2005-05-24 | 2010-08-04 | 株式会社豊田中央研究所 | 電解質 |
US7988944B2 (en) | 2005-06-28 | 2011-08-02 | Sumitomo Chemical Company, Limited | Peroxide decomposition catalyst |
JP2007012375A (ja) * | 2005-06-29 | 2007-01-18 | Toyota Motor Corp | 燃料電池、燃料電池用電極触媒層の製造方法、及び燃料電池の運転方法 |
JP5011662B2 (ja) * | 2005-07-01 | 2012-08-29 | 旭硝子株式会社 | 固体高分子形燃料電池用電解質膜の製造方法 |
CN101218700A (zh) * | 2005-07-12 | 2008-07-09 | 旭硝子株式会社 | 固体高分子型燃料电池用电解质膜、其制造方法及固体高分子型燃料电池用膜电极接合体 |
JP5217129B2 (ja) * | 2005-09-02 | 2013-06-19 | トヨタ自動車株式会社 | 燃料電池 |
JP5044909B2 (ja) * | 2005-09-07 | 2012-10-10 | トヨタ自動車株式会社 | 燃料電池 |
JP2007095433A (ja) * | 2005-09-28 | 2007-04-12 | Asahi Glass Co Ltd | 固体高分子形燃料電池用電解質膜及びその製造方法 |
JP5109244B2 (ja) * | 2005-09-29 | 2012-12-26 | 旭硝子株式会社 | 固体高分子形燃料電池用電解質膜及びその製造方法 |
US8628871B2 (en) * | 2005-10-28 | 2014-01-14 | 3M Innovative Properties Company | High durability fuel cell components with cerium salt additives |
JP2007188706A (ja) * | 2006-01-12 | 2007-07-26 | Asahi Glass Co Ltd | 固体高分子形燃料電池用電解質膜および固体高分子形燃料電池用膜電極接合体 |
US20080003476A1 (en) * | 2006-06-12 | 2008-01-03 | Virkar Anil V | Chemical additives for the suppression of catalyst degradation in fuel cells |
JP5055874B2 (ja) * | 2006-07-26 | 2012-10-24 | トヨタ自動車株式会社 | 固体高分子型燃料電池の製造方法 |
CN101606256A (zh) * | 2007-02-08 | 2009-12-16 | 住友化学株式会社 | 离子传导性组合物以及含有该组合物的离子传导膜、电极催化剂物质和燃料电池 |
JP5040437B2 (ja) * | 2007-05-21 | 2012-10-03 | トヨタ自動車株式会社 | 燃料電池 |
US8137805B2 (en) * | 2007-06-21 | 2012-03-20 | Caterpillar Inc. | Manganese based coating for wear and corrosion resistance |
JP2008098179A (ja) * | 2007-11-01 | 2008-04-24 | Asahi Glass Co Ltd | 固体高分子形燃料電池用電解質膜、その製造方法及び固体高分子形燃料電池用膜電極接合体 |
US7989115B2 (en) * | 2007-12-14 | 2011-08-02 | Gore Enterprise Holdings, Inc. | Highly stable fuel cell membranes and methods of making them |
GB0804185D0 (en) * | 2008-03-07 | 2008-04-16 | Johnson Matthey Plc | Ion-conducting membrane structures |
US8137761B2 (en) * | 2008-06-13 | 2012-03-20 | Caterpillar Inc. | Method of coating and induction heating a component |
EP2499693B1 (en) * | 2009-11-10 | 2015-09-09 | Daimler AG | Composite proton conducting electrolyte with improved additives and membrane electrode assembly for fuel cells |
JP5440330B2 (ja) * | 2010-03-31 | 2014-03-12 | Jsr株式会社 | 固体高分子電解質膜およびその製造方法、液状組成物 |
JP5023197B2 (ja) * | 2010-07-09 | 2012-09-12 | 株式会社豊田中央研究所 | 固体高分子型燃料電池 |
US20120122016A1 (en) * | 2010-11-15 | 2012-05-17 | Gm Global Technology Operations, Inc. | Fuel Cell Durability Through Oxide Supported Precious Metals in Membrane |
KR20140035965A (ko) | 2011-06-06 | 2014-03-24 | 솔베이 스페셜티 폴리머스 이태리 에스.피.에이. | 안정적인 이온 교환 불소화 중합체 및 그로부터 수득되는 막 |
JP6374382B2 (ja) | 2012-07-11 | 2018-08-15 | ソルベイ スペシャルティ ポリマーズ イタリー エス.ピー.エー. | フッ素化イオン交換ポリマー用の捕捉剤としての混合金属酸化物 |
KR102098447B1 (ko) * | 2017-06-20 | 2020-04-07 | 주식회사 엘지화학 | 고분자 전해질막, 이를 포함하는 전기화학 전지 및 흐름 전지, 고분자 전해질막용 조성물, 및 고분자 전해질막의 제조방법 |
JP2019102330A (ja) * | 2017-12-05 | 2019-06-24 | 旭化成株式会社 | 高分子電解質膜、膜電極接合体、及び固体高分子型燃料電池 |
US11575141B2 (en) * | 2020-05-28 | 2023-02-07 | Robert Bosch Gmbh | Nitrogen-doped phosphoric acid fuel cell electrolyte |
KR102510869B1 (ko) * | 2020-07-15 | 2023-03-17 | 한국과학기술연구원 | 연료전지의 전해질막용 산화방지제 및 그의 제조방법 |
CN112429813B (zh) * | 2020-09-22 | 2022-12-27 | 北京化工大学 | 一种掺杂碳纳米管的Blue-TiO2/CNT-PbO2电极材料的制备方法 |
KR102632222B1 (ko) * | 2021-07-05 | 2024-02-02 | 한국과학기술연구원 | 산화방지제를 포함하는 고분자 전해질막 연료전지용 전극, 및 이를 포함하는 막-전극 어셈블리 |
KR102504264B1 (ko) * | 2022-12-12 | 2023-02-28 | 한국과학기술연구원 | 과불소계 술폰화 이오노머용 산화방지제 및 이의 제조 방법 |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001118591A (ja) * | 1999-10-19 | 2001-04-27 | Toyota Central Res & Dev Lab Inc | 高耐久性固体高分子電解質 |
EP1271682A2 (de) * | 2001-06-27 | 2003-01-02 | BASF Aktiengesellschaft | PEM-Brennstoffzelle |
CA2396836A1 (en) * | 2001-08-09 | 2003-02-09 | Yasuaki Hidaka | Polymer electrolyte composition and fuel cell |
JP2003077492A (ja) * | 2001-09-04 | 2003-03-14 | Toshikatsu Sada | 燃料電池用プロトン導電性膜状物 |
JP2003123777A (ja) * | 2001-10-19 | 2003-04-25 | Matsushita Electric Ind Co Ltd | 高分子電解質型燃料電池 |
JP2004134294A (ja) * | 2002-10-11 | 2004-04-30 | Toyota Central Res & Dev Lab Inc | 固体高分子電解質 |
JP2004134269A (ja) * | 2002-10-11 | 2004-04-30 | Toyota Motor Corp | 高耐久性高分子電解質、同組成物、および燃料電池 |
Family Cites Families (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR1403240A (fr) * | 1964-03-13 | 1965-06-18 | Rech S Et D Applic Pour L Ind | Perfectionnements aux piles à combustible |
GB1070933A (en) * | 1964-03-13 | 1967-06-07 | Rech S Et D Applic Pour L Ind | Improvements to fuel cells |
JPS58117655A (ja) * | 1982-01-06 | 1983-07-13 | Hitachi Ltd | リン酸を電解質に用いる燃料電池 |
JPS58166645A (ja) * | 1982-03-27 | 1983-10-01 | Hitachi Ltd | 燃料電池 |
JP3356465B2 (ja) * | 1992-09-18 | 2002-12-16 | 株式会社東芝 | 固体高分子電解質型燃料電池用電極の製造方法 |
US5919583A (en) * | 1995-03-20 | 1999-07-06 | E. I. Du Pont De Nemours And Company | Membranes containing inorganic fillers and membrane and electrode assemblies and electrochemical cells employing same |
JP2000011756A (ja) * | 1998-06-22 | 2000-01-14 | Toyota Central Res & Dev Lab Inc | 高耐久性固体高分子電解質 |
CA2368896A1 (en) * | 1999-03-29 | 2000-10-05 | Siemens Aktiengesellschaft | Method for operating an htm fuel cell and htm fuel cell battery |
IT1319649B1 (it) * | 2000-11-14 | 2003-10-23 | Nuvera Fuel Cells Europ Srl | Assieme membrana-elettrodo per cella a combustibile a membranapolimerica. |
EP1382080A2 (en) * | 2000-11-30 | 2004-01-21 | MTI Microfuel Cells, Inc. | Fuel cell membrane and system with integrated gas separation |
DE10117687A1 (de) * | 2001-04-09 | 2002-10-17 | Celanese Ventures Gmbh | Protonenleitende Membran und deren Verwendung |
JP5011610B2 (ja) * | 2001-05-28 | 2012-08-29 | 株式会社豊田中央研究所 | 無機材料複合高分子膜およびその製造方法 |
JP2003151346A (ja) * | 2001-08-30 | 2003-05-23 | Sumitomo Chem Co Ltd | 高分子電解質組成物及びその用途 |
JP2003178780A (ja) * | 2001-12-11 | 2003-06-27 | Matsushita Electric Ind Co Ltd | 高分子電解質型燃料電池システム、および高分子電解質型燃料電池の運転方法 |
DE10205852A1 (de) * | 2002-02-13 | 2003-08-21 | Creavis Tech & Innovation Gmbh | Elektrolytmembran mit Diffusionsbarriere, diese umfassende Membranelektrodeneinheiten, Verfahren zur Herstellung und spezielle Verwendungen |
CA2478530A1 (en) * | 2002-03-06 | 2003-09-12 | Pemeas Gmbh | Proton-conducting electrolyte membrane with low methanol permeability and its use in fuel cells |
US7112386B2 (en) * | 2002-09-04 | 2006-09-26 | Utc Fuel Cells, Llc | Membrane electrode assemblies with hydrogen peroxide decomposition catalyst |
JP2005011697A (ja) * | 2003-06-19 | 2005-01-13 | Toyota Motor Corp | プロトン交換材料、及びプロトン交換材料を用いた燃料電池電極 |
-
2003
- 2003-08-22 JP JP2003299067A patent/JP4979179B2/ja not_active Expired - Fee Related
-
2004
- 2004-08-20 CA CA002534431A patent/CA2534431A1/en not_active Abandoned
- 2004-08-20 EP EP04772289A patent/EP1662595A4/en not_active Withdrawn
- 2004-08-20 CN CNB2004800241360A patent/CN100413135C/zh not_active Expired - Fee Related
- 2004-08-20 WO PCT/JP2004/012333 patent/WO2005020357A1/ja active Application Filing
-
2006
- 2006-02-17 US US11/356,264 patent/US20060199063A1/en not_active Abandoned
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001118591A (ja) * | 1999-10-19 | 2001-04-27 | Toyota Central Res & Dev Lab Inc | 高耐久性固体高分子電解質 |
EP1271682A2 (de) * | 2001-06-27 | 2003-01-02 | BASF Aktiengesellschaft | PEM-Brennstoffzelle |
CA2396836A1 (en) * | 2001-08-09 | 2003-02-09 | Yasuaki Hidaka | Polymer electrolyte composition and fuel cell |
JP2003077492A (ja) * | 2001-09-04 | 2003-03-14 | Toshikatsu Sada | 燃料電池用プロトン導電性膜状物 |
JP2003123777A (ja) * | 2001-10-19 | 2003-04-25 | Matsushita Electric Ind Co Ltd | 高分子電解質型燃料電池 |
JP2004134294A (ja) * | 2002-10-11 | 2004-04-30 | Toyota Central Res & Dev Lab Inc | 固体高分子電解質 |
JP2004134269A (ja) * | 2002-10-11 | 2004-04-30 | Toyota Motor Corp | 高耐久性高分子電解質、同組成物、および燃料電池 |
Non-Patent Citations (1)
Title |
---|
See also references of EP1662595A4 * |
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7943249B2 (en) | 2004-06-22 | 2011-05-17 | Asahi Glass Company, Limited | Liquid composition, process for its production and process for producing membrane-electrode assembly for polymer electrolyte fuel cells |
US10916790B2 (en) | 2004-06-22 | 2021-02-09 | AGC Inc. | Liquid composition, process for its production, and process for producing membrane-electrode assembly for polymer electrolyte fuel cells |
US10153506B2 (en) | 2004-06-22 | 2018-12-11 | AGC Inc. | Liquid composition, process for its production, and process for producing membrane-electrode assembly for polymer electrolyte fuel cells |
US9455465B2 (en) | 2004-06-22 | 2016-09-27 | Asahi Glass Company, Limited | Electrolyte membrane for polymer electrolyte fuel cell, process for its production and membrane-electrode assembly for polymer electrolyte fuel cell |
US9331354B2 (en) | 2004-06-22 | 2016-05-03 | Asahi Glass Company, Limited | Liquid composition, process for its production, and process for producing membrane-electrode assembly for polymer electrolyte fuel cells |
US8962215B2 (en) | 2004-06-22 | 2015-02-24 | Asahi Glass Company, Limited | Electrolyte membrane for polymer electrolyte fuel cell, process for its production and membrane-electrode assembly for polymer electrolyte fuel cell |
US8546004B2 (en) | 2004-06-22 | 2013-10-01 | Asahi Glass Company, Limited | Liquid composition, process for its production and process for producing membrane-electrode assembly for polymer electrolyte fuel cells |
US7879475B2 (en) | 2005-05-31 | 2011-02-01 | Kabushiki Kaisha Toyota Chuo Kenkyusho | Solid polymer electrolyte, solid polymer fuel cell and method for manufacturing the fuel cell |
EP1729361A3 (en) * | 2005-06-02 | 2008-01-09 | Mitsubishi Heavy Industries, Ltd. | Solid polyelectrolyte fuel cell |
US7670708B2 (en) | 2005-06-02 | 2010-03-02 | Mitsubishi Heavy Industries, Ltd. | Solid polyelectrolyte fuel cell |
EP1946400A4 (en) * | 2005-10-28 | 2011-01-19 | 3M Innovative Properties Co | LONG-LIFE FUEL CELL COMPONENTS CONTAINING CERIUM OXIDE ADDITIVES |
EP1946400A2 (en) * | 2005-10-28 | 2008-07-23 | 3M Innovative Properties Company | High durability fuel cell components with cerium oxide additives |
EP1970984A4 (en) * | 2005-12-28 | 2008-12-31 | Toyota Motor Co Ltd | CATALYST FOR FUEL CELL ELECTRODE, METHOD FOR MANUFACTURING SAME, FILM ELECTRODE ASSEMBLY, AND FUEL CELL |
EP1970984A1 (en) * | 2005-12-28 | 2008-09-17 | Toyota Jidosha Kabushiki Kaisha | Catalyst for fuel cell electrode, process for producing catalyst for fuel cell electrode, film-electrode assembly, and fuel cell |
US9512033B2 (en) | 2012-01-23 | 2016-12-06 | Sumitomo Electric Industries, Ltd. | Optical fiber preform |
Also Published As
Publication number | Publication date |
---|---|
JP4979179B2 (ja) | 2012-07-18 |
US20060199063A1 (en) | 2006-09-07 |
CN100413135C (zh) | 2008-08-20 |
JP2005071760A (ja) | 2005-03-17 |
CN1839503A (zh) | 2006-09-27 |
EP1662595A1 (en) | 2006-05-31 |
CA2534431A1 (en) | 2005-03-03 |
EP1662595A4 (en) | 2009-01-21 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2005020357A1 (ja) | 固体高分子型燃料電池 | |
CA2567305C (en) | Liquid composition, process for its production, and process for producing membrane-electrode assembly for polymer electrolyte fuel cells | |
US7879475B2 (en) | Solid polymer electrolyte, solid polymer fuel cell and method for manufacturing the fuel cell | |
CA2571138C (en) | Electrolyte membrane for polymer electolyte fuel cell, process for its production and membrane-electrode assembly for polymer electrolyte fuel cell | |
JP5384335B2 (ja) | イオン伝導性メンブラン | |
KR101880317B1 (ko) | 고체 고분자형 연료 전지 | |
JP4326271B2 (ja) | 遷移金属酸化物含有固体高分子電解質 | |
CN102687328A (zh) | 具有低降解性的复合质子传导膜以及包含其的燃料电池用膜电极组件 | |
JP2003086188A (ja) | 燃料電池 | |
WO2007007767A1 (ja) | 固体高分子形燃料電池用電解質膜、その製造方法及び固体高分子形燃料電池用膜電極接合体 | |
JP4972867B2 (ja) | 固体高分子形燃料電池用電解質膜、その製造方法及び固体高分子形燃料電池用膜電極接合体 | |
JP4276035B2 (ja) | 固体高分子型燃料電池用電解質膜電極接合体および固体高分子型燃料電池 | |
CN101041137B (zh) | 燃料电池的阴极催化剂以及包括它的膜电极组件和燃料电池系统 | |
JP4574149B2 (ja) | 固体高分子型燃料電池用電解質膜電極接合体および固体高分子型燃料電池 | |
JP2008198447A (ja) | 固体高分子型燃料電池 | |
JP2006134678A (ja) | 固体高分子型燃料電池及び燃料電池システム | |
JP5023197B2 (ja) | 固体高分子型燃料電池 | |
JP5568111B2 (ja) | 固体高分子型燃料電池 | |
WO2013161405A1 (ja) | 電解質膜用組成物、固体高分子電解質膜、該電解質膜の製造方法、膜-電極接合体、固体高分子型燃料電池、水電解セルおよび水電解装置 | |
JP5090717B2 (ja) | 固体高分子型燃料電池 | |
JP6963706B2 (ja) | 膜電極接合体 | |
JP2008198448A (ja) | 固体高分子型燃料電池 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
WWE | Wipo information: entry into national phase |
Ref document number: 200480024136.0 Country of ref document: CN |
|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BW BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE EG ES FI GB GD GE GH GM HR HU ID IL IN IS KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NA NI NO NZ OM PG PH PL PT RO RU SC SD SE SG SK SL SY TJ TM TN TR TT TZ UA UG US UZ VC VN YU ZA ZM ZW |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): GM KE LS MW MZ NA SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IT LU MC NL PL PT RO SE SI SK TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG |
|
DPEN | Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed from 20040101) | ||
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
ENP | Entry into the national phase |
Ref document number: 2534431 Country of ref document: CA |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2004772289 Country of ref document: EP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 11356264 Country of ref document: US |
|
WWP | Wipo information: published in national office |
Ref document number: 2004772289 Country of ref document: EP |
|
WWP | Wipo information: published in national office |
Ref document number: 11356264 Country of ref document: US |