CA1218111A - Porous gas diffusion electrode and method of producing the same - Google Patents
Porous gas diffusion electrode and method of producing the sameInfo
- Publication number
- CA1218111A CA1218111A CA000453757A CA453757A CA1218111A CA 1218111 A CA1218111 A CA 1218111A CA 000453757 A CA000453757 A CA 000453757A CA 453757 A CA453757 A CA 453757A CA 1218111 A CA1218111 A CA 1218111A
- Authority
- CA
- Canada
- Prior art keywords
- electrolyte
- respect
- copolymer
- substrate
- feed channels
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 239000000758 substrate Substances 0.000 claims abstract description 82
- 229920001577 copolymer Polymers 0.000 claims abstract description 70
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 claims abstract description 45
- 239000007789 gas Substances 0.000 claims abstract description 42
- 239000012495 reaction gas Substances 0.000 claims abstract description 37
- 238000000034 method Methods 0.000 claims abstract description 25
- 238000009792 diffusion process Methods 0.000 claims abstract description 13
- 229910052751 metal Inorganic materials 0.000 claims abstract description 11
- 239000002184 metal Substances 0.000 claims abstract description 11
- 239000003792 electrolyte Substances 0.000 claims description 48
- 239000000126 substance Substances 0.000 claims description 30
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 26
- 239000003921 oil Substances 0.000 claims description 20
- 239000000203 mixture Substances 0.000 claims description 18
- 239000000839 emulsion Substances 0.000 claims description 14
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 13
- 229910052782 aluminium Inorganic materials 0.000 claims description 11
- 238000010438 heat treatment Methods 0.000 claims description 11
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 claims description 7
- 229910010271 silicon carbide Inorganic materials 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 4
- NFFIWVVINABMKP-UHFFFAOYSA-N methylidynetantalum Chemical compound [Ta]#C NFFIWVVINABMKP-UHFFFAOYSA-N 0.000 claims description 4
- BPUBBGLMJRNUCC-UHFFFAOYSA-N oxygen(2-);tantalum(5+) Chemical compound [O-2].[O-2].[O-2].[O-2].[O-2].[Ta+5].[Ta+5] BPUBBGLMJRNUCC-UHFFFAOYSA-N 0.000 claims description 4
- RVTZCBVAJQQJTK-UHFFFAOYSA-N oxygen(2-);zirconium(4+) Chemical compound [O-2].[O-2].[Zr+4] RVTZCBVAJQQJTK-UHFFFAOYSA-N 0.000 claims description 4
- 229910003468 tantalcarbide Inorganic materials 0.000 claims description 4
- 229910001936 tantalum oxide Inorganic materials 0.000 claims description 4
- MTPVUVINMAGMJL-UHFFFAOYSA-N trimethyl(1,1,2,2,2-pentafluoroethyl)silane Chemical compound C[Si](C)(C)C(F)(F)C(F)(F)F MTPVUVINMAGMJL-UHFFFAOYSA-N 0.000 claims description 4
- UONOETXJSWQNOL-UHFFFAOYSA-N tungsten carbide Chemical compound [W+]#[C-] UONOETXJSWQNOL-UHFFFAOYSA-N 0.000 claims description 4
- 229910001928 zirconium oxide Inorganic materials 0.000 claims description 4
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 claims description 3
- 229910052731 fluorine Inorganic materials 0.000 claims description 3
- 239000011737 fluorine Substances 0.000 claims description 3
- 238000006557 surface reaction Methods 0.000 claims 2
- 239000000956 alloy Substances 0.000 claims 1
- 229910045601 alloy Inorganic materials 0.000 claims 1
- 238000010292 electrical insulation Methods 0.000 abstract description 12
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 2
- 239000001301 oxygen Substances 0.000 abstract description 2
- 229910052760 oxygen Inorganic materials 0.000 abstract description 2
- 108091006146 Channels Proteins 0.000 abstract 5
- 239000003795 chemical substances by application Substances 0.000 description 23
- 238000006243 chemical reaction Methods 0.000 description 13
- 239000002904 solvent Substances 0.000 description 13
- 238000003475 lamination Methods 0.000 description 12
- 239000000843 powder Substances 0.000 description 12
- 229910052799 carbon Inorganic materials 0.000 description 11
- 239000000835 fiber Substances 0.000 description 11
- 229910002804 graphite Inorganic materials 0.000 description 11
- 239000010439 graphite Substances 0.000 description 11
- 229910000838 Al alloy Inorganic materials 0.000 description 8
- 239000004809 Teflon Substances 0.000 description 8
- 229920006362 Teflon® Polymers 0.000 description 8
- 238000007605 air drying Methods 0.000 description 8
- 238000000137 annealing Methods 0.000 description 7
- 239000011248 coating agent Substances 0.000 description 7
- 238000000576 coating method Methods 0.000 description 7
- 230000005611 electricity Effects 0.000 description 7
- 239000008187 granular material Substances 0.000 description 7
- 239000004184 Avoparcin Substances 0.000 description 6
- 229920000180 alkyd Polymers 0.000 description 6
- 238000003756 stirring Methods 0.000 description 6
- 230000015572 biosynthetic process Effects 0.000 description 5
- 208000024891 symptom Diseases 0.000 description 5
- AJDIZQLSFPQPEY-UHFFFAOYSA-N 1,1,2-Trichlorotrifluoroethane Chemical compound FC(F)(Cl)C(F)(Cl)Cl AJDIZQLSFPQPEY-UHFFFAOYSA-N 0.000 description 4
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 4
- 239000000446 fuel Substances 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 239000006185 dispersion Substances 0.000 description 3
- 239000011888 foil Substances 0.000 description 3
- 239000002736 nonionic surfactant Substances 0.000 description 3
- 238000006116 polymerization reaction Methods 0.000 description 3
- 238000007789 sealing Methods 0.000 description 3
- BFKJFAAPBSQJPD-UHFFFAOYSA-N tetrafluoroethene Chemical group FC(F)=C(F)F BFKJFAAPBSQJPD-UHFFFAOYSA-N 0.000 description 3
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 208000003251 Pruritus Diseases 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 2
- 125000004432 carbon atom Chemical group C* 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- 239000010408 film Substances 0.000 description 2
- ZZUFCTLCJUWOSV-UHFFFAOYSA-N furosemide Chemical compound C1=C(Cl)C(S(=O)(=O)N)=CC(C(O)=O)=C1NCC1=CC=CO1 ZZUFCTLCJUWOSV-UHFFFAOYSA-N 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- -1 perfluoroalkyl vinyl ether Chemical compound 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 206010013642 Drooling Diseases 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 241000490229 Eucephalus Species 0.000 description 1
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical group F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 1
- 241000282320 Panthera leo Species 0.000 description 1
- 206010037660 Pyrexia Diseases 0.000 description 1
- 208000008630 Sialorrhea Diseases 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- UUAGAQFQZIEFAH-UHFFFAOYSA-N chlorotrifluoroethylene Chemical group FC(F)=C(F)Cl UUAGAQFQZIEFAH-UHFFFAOYSA-N 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 229920001038 ethylene copolymer Polymers 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 150000002222 fluorine compounds Chemical class 0.000 description 1
- 125000001153 fluoro group Chemical group F* 0.000 description 1
- NBVXSUQYWXRMNV-UHFFFAOYSA-N fluoromethane Chemical compound FC NBVXSUQYWXRMNV-UHFFFAOYSA-N 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 238000000265 homogenisation Methods 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000010977 jade Substances 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 238000010030 laminating Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 125000005010 perfluoroalkyl group Chemical group 0.000 description 1
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 1
- 239000004810 polytetrafluoroethylene Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 239000000565 sealant Substances 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
- H01M8/0271—Sealing or supporting means around electrodes, matrices or membranes
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M12/00—Hybrid cells; Manufacture thereof
- H01M12/02—Details
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/10—Primary casings; Jackets or wrappings
- H01M50/183—Sealing members
- H01M50/19—Sealing members characterised by the material
- H01M50/193—Organic material
-
- 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
- Y02E60/10—Energy storage using batteries
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Fuel Cell (AREA)
- Laminated Bodies (AREA)
Abstract
ABSTRACT OF THE DISCLOSURE
A porous gas diffusion electrode for use in an air-metal cell or a hydrogen-air (oxygen) cell compris-ing an electroconductive porous substrate, which has itself on one surface thereof reaction gas feed channels or is to be used with one surface in contact with reac-tion gas feed channels during use, and which comprises gas impermeable and electrically insulating seals formed of a tetrafluoroethylene-perfluoroalkyl vinyl ether copolymer provided on the substrate at least at both end portions parallel to said reaction gas feed channels, is capable of positively shielding the gas streams at the end portions parallel to the reaction gas feed chan-nels and maintaining electrical insulation.
Such a porous gas diffusion electrode can be pre-pared by a method comprising applying a tetrafluoroethylene-perfluoroalkyl vinyl ether copolymer on the substrate at least at the end portions parallel to the reaction gas feed channels and then subjecting the substrate coated with the copolymer to hot pressure bonding by means of a pressure bonding tool made of a metal previously coated with a fluoride oil to form gas impermeable and electrically insulating seals comprising said copolymer.
A porous gas diffusion electrode for use in an air-metal cell or a hydrogen-air (oxygen) cell compris-ing an electroconductive porous substrate, which has itself on one surface thereof reaction gas feed channels or is to be used with one surface in contact with reac-tion gas feed channels during use, and which comprises gas impermeable and electrically insulating seals formed of a tetrafluoroethylene-perfluoroalkyl vinyl ether copolymer provided on the substrate at least at both end portions parallel to said reaction gas feed channels, is capable of positively shielding the gas streams at the end portions parallel to the reaction gas feed chan-nels and maintaining electrical insulation.
Such a porous gas diffusion electrode can be pre-pared by a method comprising applying a tetrafluoroethylene-perfluoroalkyl vinyl ether copolymer on the substrate at least at the end portions parallel to the reaction gas feed channels and then subjecting the substrate coated with the copolymer to hot pressure bonding by means of a pressure bonding tool made of a metal previously coated with a fluoride oil to form gas impermeable and electrically insulating seals comprising said copolymer.
Description
~18~1~
POROUS GAS DIFFUSION ELECTRODE AND
METHOD OF PRODUCT IN TOE SUE
BACKGROUND OF THE INVENTION
ethnical Field of the Invention This invention relates to a porous was diffusion electrode and a method of preparing the same and Gore particularly to a porous gas diffusion electrode provided with end portion seals constituting an electricity generating element which can ye used ion air-metal cells and fuel cells, be easily laminated, and used with high reliability and also to a method of producing the same.
Technical Background of the Invention and its Problems Air-metal toe cells or hydro~Jen-air (oxygen) fuel cells are required to have electrodes for ionization of was as their electromotive mechanisms. The gas Defoe-soon electrode, in which a was having no electroconduc-tivity participates continuously in electromotive reaction, em toys a porous plate substrate and is so constituted that one surface of the substrate is brought into contact with an electrolyte, and the gas Lyon into the substrate from the other surface is permitted to participate in the electromotive reaction within the substrate. In general, for feeding a reaction was, reaction gas feed channels are provided on the substrate itself/ or the substrate it used so as to be contacted with another element having reaction was feed channels.
In these cell systems, each unit cell outputs a voltage of at most 0.5 to 1.5 V, end hence a considerable number of unit cells are required to be laminated and provided for practical use. Turing lar.lination,unit cells are laminated in such a manner that the reaction was feed channels provided on one substrate itself or provided in contact with the substrate during use under lamination are in a direction -to cross over other was feed channels provided avow or bullet ccordinqly, it 'I
is necessary to treat the end portions on the side faces parallel to the respective gas feed channels so that one reaction was, for example, h~droyen was, flowing through one reaction was channel and another was, for example, air, flowing through another gas feed channel above or under said channel will not become mixed with each other. At the same tire, it is also necessary to treat the end portions so as to maintain electrical insulation even when compressed mechanically strongly by lamination of a large number of units.
In order to prevent mixing of different vases at the end portions of the substrate parallel to was feed channels and to ensure electrical insulation at the end portions, a method in which the end portions are coated with synthetic resins and a method in which the are impregnated with a dispersion of a tetrafluoro-ethylene copolymer have been proposed. However, none of these methods have been successful in obtaining satisfactory results.
SEYMOUR OF THE INVENTION
Accordingly, an object of the present invention is to provide a porous gas diffusion electrode for use in an air-metal cell or a hydro~en-air loden cell comprising an electroconductive porous substrate, which has itself on one surface thereof reaction gas feed channels or is to be used with one surface in contact with reaction was feed channels during usage, the electrode briny capable ox positively shielding the gas streams a-t the end portions parallel to the react lion was feed channels end maintaining electrical insulation. Another object of the invention is to provide a method of preparing such an electrode.
In accordance of the present invention, there is provided a porous was diffusion electrode comprising an electroconductive porous substrate, which has itself on one surface thereof reaction gas feed channels or is to be used with one surface in contact with reaction I
gas feed channels during use, and which comprises was impermeable and electrical insulating seals formed of a tetrafluoroethylene-perfluoroalkyl vinyl ether copolymer (hereinafter sometimes referred to as PEA
copolymer) provided on the substrate at least at both end portions parallel to said reaction gas feed channels.
The present invention also provides a method of preparing such a porous gas diffusion electrode, itch method comprises applying a tetrafluoroethylene-perfluoroalk~71 vinyl ether copolymer on the substrate at least at the end portions parallel to the reaction gas feed channels and then subjecting the substrate coated with the copolymer to hot pressure bonding by means of a pressure bonding tool jade of a metal pro-piously coated with a fluoride oil to form gas impermeable and electrically insulating seals comprise in said copolymer.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 is a perspective view of an electricity generating element including a porous gas diffusion electrode having formed seals at the end portions according to the resent invention;
FIG. 2 through 4 are schematic perspective views : respectively of the states under hot pressure bonding in a mold cavity according to the method of the present invention, wherein FIG. 2 shows the case of use of powdery or granular coupler, FIG. 3 the case of use of film copolymer, and FIG. 4 the case of use of powdery or granular copolymer and film copolymer; and FIG. 5 is a schematic illustration of the state under hot pressure bonding of a substance wettable with an electrolyte and stable thermally and chemically with respect to the electrolyte, which is further applied on the fused portion of PEA copol~f~mer.
DETAILED DESCRIPTION OF THE INVENTION
In on embodiment of the present invention as shown in FIG. 1, the electric power generating element I
comprises, in the order from above, an electrode 1 provided with reaction gas weed channels I, an electron lute layer 2, a thin electrode 3 and a laminated element provided with reaction gas feed channels 6.
The several reaction was feed channels 5 provided in the electrode 1, and the reaction gas feed channels 6 provided in the laminated element 4 are perpendicular - to each other.
- For both of the electrodes 1 and 3, porous sup-striates with a porosity of 60 to 70 which are plate shaved an are electron conductive are used. For eagle porous plates prepared by forming sistered nickel or graphite fibers into paper and then heat treating, the same can be used. The latter is suitable in a fuel cell in which a concentrated acid liquid such as gone.
phosphoric acid is used as the electrolyte.
In the present invention, at the end portions of such electrodes 1 and 3, gas impermeable, electrically insulating seals are provided. As shown in FIG. 1, in the electrode 1 provided with the reaction gas feed channels 5, these seals are provided at the end portions 7, 7 in parallel to the reaction was feed channels, while in the thin electrode 3, the are provided at the end portions 8, 8 in parallel to the reaction gas feed channels 6 provided in the laminated element I in contact with the thin electrode upon lamination. In the thin electrode 3, it is also possible to provide seals at other orations such as the end portions crossly over the channels 6, but it is necessary to provide the seals at least at the end portions 8, 8 in parallel to the channels 6.
For formation of the aroused seal, it is necessary to use a material which is capable of sealing the fine pores in the end portions to prevent passage or leak of reaction gases therethro~h and also main-lain electrical insulation in spite ox the mechanical pressure during lamination, end which has excellent . , I
chemical resistance so as to withstand hick temperature actions with the use of a concentrated acidic electron lyre and is thermally stable at temperatures in excess of 250C, even at a temperature of 350C for a short period of time. The material must also have heat-sealable property. As such a material, a tetrafluoro-ethyl-perfluoroalkylvinylether copolymer is used.
Tetrafluoroethylene has the molecular formula of CF2=CF2, as is well known in the art, and perfluoroalkyl vinyl ether the formula of SHAKER, wherein R represents a perfluoroalkyl group having ordinarily 2 to 4, preferab-lye 3, carbon atoms, of which the hydrogen atoms on the alkyd group are all substituted with fluorine atoms. The content of tetrafluoroethylene in this copolymer are with-in the range of from about 96 to 97 by weight.
This copolymer is commercially available in the form of powder, granules, film and emulsion. These forms can be used either singly or in any desired combination. For example, the above copolymers in the form of powder or granules can be dispensed on the surface at the end portions and then subjected to pressurization into the porous substrate by application of heat and pressure, or a film of the above copolymer can be covered all over the end portions, namely in U-shape, and then subjected to application of heat and pressure thereon to cause the film to be closely contacted by the porous substrate ends, thereby forming seals.
It is also possible to disperse the above Capella-men in the form of powder or granule on the surfaces of the end portions, then cover the surfaces with a film of the above copolymer, and apply heat and pressure to the film to form seals. alternatively, the surfaces of the end portions can be coated with the copolymer in state of emulsion, and then heat and pressure applied thereto, or further a film of the copolymer can be placed thereon, tush step is followed by a similar :
application of heat and pressure to form seals.
The method of forming the end portion seals on such porous gas diffusion electrodes 1 and 3 isle nudge - be described in treater detail. The above mentioned copolymer in the form of powder or granules is mixed with a suitable solvent such as one of fluoride type and stirred at room temperature to 40C to prepare a mixed agent. This mixed agent is applied on the surfaces of the end portions of the porous substrate constituting the electrode and dried in air to cause the powdery or granular copolymer to be dispersed evenly throughout the surfaces of the end portions, Its amount is such that there will be a rise of the sealant of about 0.1 to 0.3 em after hot pressure bonding and air drying. Then, the substrate is placed within a female mold of a pressure bonding tool made, of a metal such as a mold cavity coated previously with a mold releasing agent comprising a fluoride oil, and a male mold is placed against the surfaces of the end portions having the above copolymer dispersed therein. Then pressure bonding is carried out while heating the whole assembly to a temperature not higher than 380C, preferably 340 to 350C under pressurize-lion ox about 20 to 40 kg/cm2 in terms of planar pressure.
As the fluoride oil, co~ercially available fluoride wax may be used as it is, or this may be further idea with a fluoride solvent under stirring before use. What is important here is that at least 3Q the necessary portions on the surface ox the pressure bonding tool, namely, the portions to be contacted by the portions on which the above copolymer is dispersed or deposited, should previously be coated with a fluoride oil as a told releasing agent. it is also 'I 35 important to control the temperature to a value not higher than 380C. Since the above copolymer has good heat-sealable property with respect to a petal, told ;
release can be easily carried out with tune use of a fluoride oil as the mold releasing agent. On tune other hand, the above powclerv or granular copolYmer will begin to generate bubbles at a temperature in excess of 380C, whereby uniform formation of seals is rendered impossible. In practice, heating is carried out at a temperature of 340 - 330C under the planar pressure mentioned above for 15 to 30 minutes, and then annealing is conducted at 80 to 90C for about one hour, followed by removal of the sealed product from the mold.
This method is indicated in FIG. 2, in itch a powdery of granular copol~tmer 11 is disperse on the surfaces of a porous substrate 10 for formation of an electrode, at the end portion thereof. On the other hand, the mold is previously coated with a mold releasing agent comprising a fluoride oil at the corner portion of a female mold 12 and the pressure bonded face of a male mold 13, namely at the sites to be contacted with the surface where the above copolymer is dispersed. As illustrated in the drooling, the porous substrate 10, on which the above copolymer 11 is dispersed in an amount such that it Lyle be raised to about 0.1 to 0.3 mm after air clarion, is placed within the female mold 12 previousltl/ coated with the fluoride oil motel releasing agent, and then hot pressure bonding is carried out by means of the male mold similarly coated with the mold releasing agent 14 by pressurization from upward and downward directions A and B.
In the case where the above calmer is used in the form of a film, oration of the seal is possible in substantially the save manner. More specie ficall~r, as shown in FIG. 3, the above calmer 15 in the form of a film with a thickness of about 0.1 to 0.2 mm is placed as a cover on the surface of thy end portion of the porous substrate 10 with a Ushered cross-section, and the covered substrate is placed within the female mold 12 coated previously with a fluoride oil mold releasing agent I after which hot pressure bonding is carried out by pressurization from both upward and downward directions. Also, in this case, the heating temperature must not exceed 380C, and a good seal portion can be for~ecl in practice by heating to 340 to 380C under pressurize-lion of a planar pressure of about 20 to 40 k~/cm2 for 15 to 30 minutes and then performing annealing at a temperature of 80 - 90C for about one hour, thereby pressurizing the above coupler into the porous substrate.
Referring no to FIG. I, here the powdery or granular copolymer 11 is dispersed first similarly as described above on the surface of the end portions of the porous substrate 10, and further the cooolvmer 15 in form of a film with a thickness as specified above is placed there over as a cover before placement of the substrate within a female told 12 coated previously at the necessary portion With a fluoride oil 14. Then hot pressure bonding is carried out under the save pressure and temperature conditions as described above. It is also possible to disperse first the powdery or granular polymer, which is then subjected to hot pressure bonding to be pressurized into the porous substrate, and then to place a film copolymer as a cover over the substrate and carry out hot pressure bonding again.
In addition, a copolymer in the state of an emulsion can be applied on the surface of a porous substrate an dried, after josh it is subjected to hot pressure bonding in a motel to be pressurized into the porous substrate. Alternatively, as described above, aster coating an drying, a film copolymer can be place as a cover over the substrate, and there-after hot pressure bonding can be carried out. Such I
g a copolymer in the state of an emulsion can ye pry' by, for example, adding 100 parts by weight of -Atari and 1 to 5 parts by weight of a non ionic surfactant to 20 to 60 parts by weight of the powdery or granular copolymer and vigorously stirring the mixture.
As described above, PEA copolymer is commercially available in various forms such as powder, granules, film, emulsion, etc., and can be used in any desired form. When PEA copolymer in the form of a film is employed, the copolymer can be previously formed in the shape of the letter U in cross-section so as to correspond to the shape of the aforesaid end portion, and the formed film is placed over the entire end portion, which step is followed by application of heat and pressure to obtain close contact of the film against the end portions of the porous substrate to -form seals. By this process, improvement ox yield can be brought about.
Alternatively, it is also possible to form seals by dispersing or applying the aforesaid copolymer in the form of powder, granules or emulsion on the surface of the end portions before placing the above copolymer molded in a film there over, and then applying heat and pressure to the film.
More specifically, the above copolymer in the form of flat film is relatively hard, and therefore it is not easily placed over the end portion. Accord-tingly, the film employed is previously heated to 20Q
to 230C and molded by means of a working tool into a U-shape in cro~s-section corresponding to the end portion. PEA copolymer in the form of a molded film is placed as a cover over the end portion of a porous substrate. The cowered substrate is then placed in a female mold of a pressure bonding tool ox a metal sun as a mold cavity made of aluminum or an aluminum alloy having a smooth surface coated previously with a mold releasing agent comprising a fluoride oil, and a male ~2~L81~1 mold coated similarly on the surface of the end portion with a mold releasing agent is pressed against the covered substrate. Finally, this step is foolhardy by heating under pressurization at a temperature within the range of from 340 to 350C for 15 to 30 minutes to accomplish hot pressure bonding.
As the fluoride oil, commercially available fluoride wax may be used as it is, or a mixture of such a wax can be further mixed with a fluoride solvent under stirring before use. What is important here is to employ a working -tool having a smooth surface made of aluminum or an aluminum alloy, in view of the fact that the above copolymer having a generally good heat-seal property with respect to metals was found by experiment to be difficult to attached by melting to aluminum or an aluminum alloy, and to coat previously, the necessary portion of the worming tool, namely, the portion contacted by the covered portion of the above copolymer,with a mold releasing agent. It is also important not to elevate the temperature above 380C.
The working tool for pressure bonding made of aluminum or an aluminum alloy is not limited to those made wholly of aluminum metal or aluminum alloy, but it is also possible to use favorably one which is coated on the surface corresponding to the bonded portion with â
foil of aluminum metal or an aluminum alloy.
Further, in the present invention, after formation okay' the hot pressure bonded portion of PEA copolymer at the end portion of a porous substrate, a substance that -is wettable With an electrolyte and is thermally and chemically stable with respect to an electrolyte can be provided by not pressure bondincJ to Norm a gas , impermeable and electrically insulating seal formed of PEA copolymer and the aforesaid substance at the end portion, whereby it is possible to obtain an electrode which is wettable with an electrolyte between the electrodes, is capable ox retaining an ample amount of the electrolyte in the electrolyte layer and further has an end portion seal with reliability. examples of the substance used here are silicon carbide, titanium carbide, tantalum carbide, tungsten carbide, zirconium oxide, tantalum oxide, and carbon powder.
These may be used either singly or as any combination thereof. Any of these substances exhibits good nettability with respect to an electrolyte and is chemically stable without being corroded by the electrolyte. It is also stable at high temperatures of about 200C or higher at which the fuel cell employing the electorate operates. This substance is ordinarily employed in the form of powder or granules.
The place where this substance is pressure bonded under heating may be the whole fused portion of PEA
copolymer formed in the shape of U in cross-section ; on the end portion of the substrate as described above, but the substance is applied by hot pressure bonding on the fused portion of PEA copolymer at least on the side opposite to the surface having the aforesaid reaction gas feed channels or opposite to the face to be in contact with the reaction gas feed channels when used under lamination.
- US In practicing hot pressure bonding of such a substance, as shown in FIG. 5, on the surface of the fused portion 18 formed at the end portion of the porous substrate 17 having reaction gas feed channels on one surface, at least on the face opposite to the face having the reaction gas feed channels 16, a substance 19 wettable with an electrolyte and thermally and chemically stable with respect to the electrolyte is dispersed densely to a thickness of about 0.05 to 0.3 mm, which is then subjected to hot pressure bond-in by means ox a hot pressure bonding tool made of metal such as aluminum as shown in FIX. 2 while being heated to a temperature ox 300 to 370C under a planar ,.
I"
Jo pressure similarly as described above.
The substance wettable with an electrolyte and thermally and chemically stable with respect to toe electrolyte as mentioned above may be used solely, but it can be also used in the form of a mixture with the above PEA copolymer or in the form of a paste e mixture prepared by mixing the three components of the substance, the above PEA copolymer and a fluoride type dispersing medium. The proportions are preferably 3 10 to 40 parts by weight of PEA copolymer powder per 100 parts by weight of the above substance in the former case, while the proportions are preferably 3 to 40 parts by weight of PEA copolymer powder and 150 to 600 parts by weight of a fluoride type dispersing medium per 100 parts by weight of the above substance in the latter case. The conditions during hot pressure bonding such as the temperature are substantially the same as in the case where the above substance along is used.
Thus, the porous gas diffusion electrode obtained according to the present invention by forming gas impermeable, electrically insulating seals comprising a tetrafluoroethylene-perfluoroalk~l vinyl ether copolymer at least at both end portions parallel to the reaction gas feed channels of a porous substrate not only can prevent completely leakage of reaction gas from the end portions but also will not be broken under strong pressure during lamination of electricity generating elements such as these electrodes due to its mechanical reinforcement, having also good electrical insulating property or complete prevention of semi-short circuiting at the end portions frequently occu~rinq in tune past. Also, since lamination of electricity generating elements has been simplified, toe time needed for laminating assembly thereof can be shortened to a great extent and high reliability of the lam-noted product can be maintained. In this connection, I
. .
when electricity generating elements were formed by tune use of a porous substrate subjected to treatment of the end portions with a polytetrafluoroethylene suspension, the yield was only about 2/5 as compared with the case in which the electrode of the present invention was employed, and lamination was also difficult. Thus, the present invention has also additional merits such as improvement of yield to a great extent.
If the above copolymer in the form of a flat film which is not contour able along the shape of the end portion is employed, it cannot be set well in position in the shape of the end portion, for example, a U-shaped cross-section, whereby the yield after hot pressure bonding will become only 50 to 60 I. By permitting the above copolymer film to substantially coincide in shape with the end portion, for example, molding the film to have a U-shaped cross-section, and carrying out hot pressure bonding with the molded film covering the end portion, the yield can be improved to 30 to 90 %.
Further, by making the surface of the working tool for hot pressure bonding of smooth aluminum or aluminum alloy, no melt adhesion of the copolymer to the mold cavity will occur, whereby a yield close to 100 % can be attained.
; 25 Also, by further applying a substance wettable with an electrolyte and thermally, chemically stable with respect to the electrolyte by hot pressure bonding on the surface of the fused portion obtained by hot pressure bonding of PEA copolymer at both end portions parallel to the reaction gas feed channels on a porous plate substrate, at least on the surface of the fused portion on the side opposite to the face having the reaction gas feed channels or on the side oppose e to the face to be contacted with the reaction gas feed channels when laminated, the aforesaid suffuse can ` exhibit nettability with an electrolyte such as pros-phonic acid, whereby a sufficient amount of electrolyte I, .., can be held in the electrolyte layer between electrodes, and the leak of reaction gas can be prevented. The above substance, and toe fused portion will not be peeled off, and of course the seal can withstand the strong pressure during lamination without incurring breakage thereof to maintain its good electrical insulation, thus providing a porous electrode having end portion seals which are reliable.
Example 1 A mixture of 192 g of a tetrafluoroethyleneperfluoro-alkyd vinyl ether copolymer (Teflon MP-20, trade mark, produced by Mets Fluorochemical Co., Ltd.) and 128 g of a fluoride type solvent (Flurried FC 721, trade mark, Symptom EM Co., Ltd.) was stirred at room temperature for 30 minutes to prepare a mixed agent for coating.
Then, a porous plate substrate made of thin graphite fibers comprising a carbon paper with a size of 700 my x 700 mm and a thickness of 0.5 mm (E-715, trade mark, produced by Zaire Kagaku Co., Ltd.) was coated at both end portions with the above mixed agent to widths each of 20 mm and left to stand for air drying to cause the above copolymer to be dispersed at said end portions.
Separately, a mold as shown in the drawings was previously coated at the necessary portions with a fluorine wax ; (Difloil #100, trade mark, produced by Osaka Kinesic Kiwi Co., Ltd.), and the porous substrate as prepared above was placed within the mold, and heated at a temperature of 340 to 370C under a load of a planar pressure of 20 kg/cm2 for about 15 minutes, after which annealing was carried out at 80 to 90C for about one hour.
When the mold was removed, and the product was left to stand for air drying, the above copolymer was found to be pressurized into the substrate and attached with a rise of about 0.1 mm.
The sealed portion thus formed was uniform at the end face without any leakage of gas whatsoever, was mechanically strengthened after lamination, and had good electrical insulating property.
Example 2 A mixture of 192 g of a tetrafluoroethyleneperfluoro-alkyd vinyl ether copolymer (Teflon MP-10, trade mark, produced by Mets Fluorochemical Co., Ltd.) and 128 g of a fluoride type solvent (Dillon Solvent So, trade mark, produced by Osaka Kinesic Cage Co., Ltd.) was stirred under heating at 45 to ~0C for 30 minutes to prepare a mixed agent for coating.
Then, by using as the substrate a carbon paper with a size of 700 mm x 700 mm and a thickness of 2 mm (E-750, trade mark, produced by Query Kagaku Jo., Ltd.3 prepared by she~t-making of graphite fibers, the substrate was coated at both end portions with the above mixed agent to widths Mach of 20 mm and left to stand for air drying to cause the above copolymer to be dispersed at the end portions.
Separately, with the use of a mold releasing agent prepared by homogenization of a mixture of 120 g of a fluoride wax (Difloil #100, trade mark, produced by Osaka Kinesic Kiwi Co., Ltd.) and 180 g of a fluoride solvent (Freon 113, trade mark, produced by Mets Fluorocnemical Co., to by stirring at 45 to 50C for 30 minutes, a mold was coated at necessary portions with the mold releasing agent The above porous substrate was placed in or I, the mold and subjected to hot pressure bonding similarly as described in Example l. The above copolymer was found to be pressurized into the substrate and attached after air drying with a rise of about 0.3 mm on the surface. A sealed portion with excellent gas impermeability and electrical insulation was formed, whereby leakage of gas could be completely prevented.
Example 3 A porous plate substrate of thin graphite fibers comprising a carbon paper with a size of 700 mm x 700 mm and a thickness of 0.5 mm (E-715, trade mark, produced by Query ~agaku Cage Co., Ltd.) was coated at the end portions with a film of a tetrafluoroethylene-perfluoro-alkyl vinyl ether copolymer (PEA
500 LO, trade mark, produced by Mets Fluorochemical Co., Ltd.) with a width of 20 mm and a thickness of 0.13 mm in the shape of U.
Then, the above porous substrate was placed in a mold previously coated at the necessary portions with a fluoride wax (Difloil #100, trade mark, produced by Osaka Kinesic Cage Co., Ltd.), and subjected to hot pressure bonding by heating at a temperature of 350 to 370C under a load of a planar pressure of 20 kg/cm or about 30 minutes, annealing at 80 to 90C for about one hour, and removal from the mold to complete the end portion sealing. The end portion seal thus obtained was found to be uniform at the end surface, and there was no gas leakage whatsoever from this portion.
Example _ A mixture of lg2 g of a powdery tetrafluoroethylene-perfluoroalkyl vinyl ether copolymer (Teflon HP-20, trade mar, produced by Mets Fluorochemical Co., Ltd.) and 128 g of a fluoride .......
I'.. .' I
.
~2~B~
type solvent (Flurried FC 721, trade mark, Symptom I co ., ~td.3 aye stirred at room temperature for 30 minutes to prepare a mixed agent for coating.
Then, a porous plate substrate made of thin graphite fibers which was a carbon paper with a size of 700 mm x 700 mm and a thickness of 2 mm (E-750, trade mark, produced by Query Kagaku Co., Ltd.) was coated at both end portions with the above mixed agent to widths each of 20 mm and left to stand for air drying, which step was followed by further coating with a film of a twitter-fluoroethylene-perfluoroalkyl vinyl ether copolymer (PEA 500 LO, trade mark, produced by Mets Fluorochemical Co., Ltd.) with a width of 30 mm and a thickness ox 0.13 mm in the shape of U.
Separately, a fluoride oil was prepared by mixing 120 g of a fluoride wax (Difloil ~100, trade mark, produced by Osaka Kinesic Cage Co., Ltd.) and 180 g of a fluoride solvent Freon 113, trade mark produced by Mets Fluorochemical Co., Ltd.) under stir-ring at 45 to 50C for I minutes. The above porous substrate have in the powdery and film copolymers dispersed or coated at the end portions as described above was placed in a mold, which had been previously coaxed with thy fluoride oil, and subjected -to hot pressure bonding under the same conditions as in Example 3 to form end portion seals.
From the end portion seals thus formed, there was no gas leakage whatsoever, the end surface being smooth. Particularly no deterioration was detected in a cell prepared ho lamination of the electricity generating elements containing the electrodes obtained by the use of this seal after operation at a high -temperature for a long time. The result was also similar with respect to electrical insulation.
aye Example 5 To 40 parts by weight of a tetrafluoroethylene-perfluoroalkyl vinyl ether copolymer (Teflon MP-20, trade mark, produced by Mets Fluorochemical Co., Ltd.) were added 100 parts by weight of water and 3 parts of a non ionic surfactant (Briton X-100, trade mark, produced by Room Hays Japan Co,, Ltd.), and the mixture was vigorously stirred for dispersion of the above copolymer thereby to prepare an emulsion thereof.
As the next step, a porous plate substrate made of thin graphite fibers comprising a carbon paper with a size of 700 mm x 700 mm and a thickness of 0.5 mm (E-715, trade mark, produced by Query Kagaku Co., Ltd.) was coated at both end portions with the above emulsion to widths of 20 mm and dried.
Then/ hot pressure bonding was carried out in a mold coated with a fluoride oil similarly as in Example 1. As a result, seal portions having good electrical insulation without gas leakage from the end surfaces were similarly obtained.
Example 6 An emulsion of the tetrafluoroethylene-perfluoro-alkyd vinyl ether copolymer was prepared in the same manner as in Example 5, and the thin carbon paper was coated with this emulsion and dried. This was further coated with a film of tetrafluoroethylene-perfluoro-alkyd vinyl ether copolymer (PEA 500 LO, trade -ye, produced by Mets Fluorochemical Co., Ltd.) with a thickness of 0.13 mm in shape of U.
Following thereafter the same procedure as in Example 1, hot pressure bonding was carried out under the same conditions in a mold coated with the fluoride oil. As a result, sealed portions having excellent gas impermeability and electrical insulation property were formed.
Example 7 _ A porous plate substrate of thin graphite fibers comprising a carbon paper with a size of 700 mm 700 mm 25 and a thickness of 0.5 mm (E-715, trade aye, produced by Query Kagaku Cage Cowl Ltd.) was provided at the end portions to widths each of 20 mm with a film of a tetrafluoroethylene-perfluoroalkyl vinyl ether copolymer (PEA 500 LO, trade-n~ffl~, produced by Mets Flyer-chemical Co., Ltd.) with a thickness ox 0.13 em which had been molded in the shape substantially corresponding to the end portion by softening in a mold heated at 220 - 230C.
Then, the mold surface ox the hot pressure bond-in tool was covered with an aluminum foil, and the above porous substrate was placed in a mold previously coated at the necessary portions with a fluoride way (Difloil #100, trade mark, produced by Osaka Xinzoku Cage Coy, Ltd.), and subjected Jo hot pressure bonding by heating at a temperature of 350 - 370C under a load of a planar pressure of 20 kg/cm2 for about 30 minutes, annealing at 80 - 90C for about one hour, and removal from the mold to complete the end portion sealing. The end portion seal thus obtained was found to be uniform at the end surface without any gas leakage.
Example 8 mixture of 192 g of a powdery tetrafluoroethylene-perfluoroalkyl vinyl ether copolymer (Teflon HP-20, trade mark, produced by Mets Fluorochemical Co., Ltd.) and 128 g of a fluoride type solvent (Flurried FC 721, trade mark, Symptom EM Co., ; Ltd.) was stirred at room temperature for 30 minutes to prepare a mixed agent for coating.
Then, by using as the porous plate substrate a carbon paper with a size of 700 mm x 700 mm and a thickness of 2 mm (E-750, trade mark, produced by Query Kagaku Co., Ltd.) prepared by sheet making of graphite fibers, the substrate was coated at end portions with the above mixed agent to widths of 20 mm and dried in air end further provided with a film of a tetrafluoroethyl-ene-perfluoroalkyl vinyl ether copolymer (PEA 50Q LO, trade mark, produced by Mets Fluorochemical Co., Ltd.) with a thickness of 0.13 mm which had previously been formed into a U-shape similarly as described in Example 7.
Separately, a fluoride oil was prepared by mixing 120 g of a fluoride wax (~ifloil #100, trade mark, produced by Osaka Kinesic Cage) and 180 g of a fluorine solvent Freon 113, trade mark, produced by it's Fluorochemical Co., Ltd.) under stirring I
at 45 - 50C for 30 minutes. The above described porous substrate having the powdery and film copolymers dispersed or coated at the end portions as described above was placed in a mold, which had been previously coaxed with the fluoride oil, and subjected to hot pressure bonding under the same conditions as in Example 7 to form end portion seals.
From the end portion seals thus formed, there was no gas leakage whatsoever, the end surface being smooth. Particularly, no deterioration way detected in a cell prepared by lamination of the electricity generating elements containing the electrodes obtained by the use of this seal after operation at a high temperature for a long time. The result was also similar with respect ; to electrical insulation.
Example 9 .
To 40 parts by weight of a tetrafluoroethylene-perfluoroalk.yl vinyl ether copolymer (Teflon MP-~0, trade mark, produced by Mets Fluorochemical Co., Ltd.) were added 100 parts by weight of water and 3 parts of a non ionic surfactant Briton X-100, trade mark, produced by Room & Hays Japan Co., Ltd.), and the mixture was vigorously stirred for dispersion of the above Capella-men, to prepare an emulsion thereof.
As the next step r a porous plate substrate made of thin graphite fibers comprising a carbon paper with a size of 700 mm x 700 mm and a thickness of 0.5 mm (E-715, trade mark, produced by Query Kagaku Co., Ltd.) was coated at both end portions with the above emulsion to widths each of I mm and dried.
Subsequently, a film of a tetrafluoroethylene-perfluoroalkyl vinyl ether copolymer (PEA 500 LO, trade mark, produced by Mets ,,,,'~ ~72_ Fluorochemical Co., Ltd.1 with a thickness of 0.13 em was formed into a U-shape similarly as described in Example 7, and the end portions of the above coated substrate were inserted whereinto.
Then, hot pressure bonding was carried out in a mold formed of Solomon, which is an aluminum alloy, coated with a fluoride oil similarly as in Example 7 under the same conditions.
As a result, seal portions of excellent gas impermeability and electrical insulation property were obtained.
Example 10 A mixture of 192 g of a tetrafluoroethylene-perfluoro-alkyd vinyl ether copolymer (PEA copolymer) (Teflon MP-20, trade mark, produced by Mets Fluorochemical Co., Ltd.) and 12~ g of a fluoride type solvent (Flurried FC 721, trade mark, Symptom EM Co., Ltd.) was stirred at room temperature for 30 minutes to prepare a mixed agent for coating.
Then, a porous plate substrate made of thin graphite fibers comprising a carbon paper with a size of 700 mm x 700 mm and a thickness of 0.5 mm EYE, trade mark, produced by Query Kagaku Co., Ltd.) was coated at both end portions with the above mixed agent to widths lack of 20 mm and left to stand for air drying to cause the above copolymer to be dispersed at said end portions.
Separately, a mold as shown in the drawings was pry-piously coated at the necessary portions with a fluoride wax (Difloil #100, trade mark, produced by Osaka Kinesic Cage Co., Ltd.), and the porous substrate a prepared above was placed within the mold and heated at a temperature of 34Q - 370~C under a load of a planar pressure of 20 kg/cm2 for about 15 minutes, which step . ..
,, I.
I
aye was followed by annealing at 80 - 90C for about one hour. r~rnen the mold was removed, and the product was left to stand for air drying, the above copolymer was found to be pressurized into the substrate and the thermally fused portion of PEA copolymer formed, being attached with a rise of about 0.1 mm.
Having thus formed the thermally fused portions of PEA copolymer at the ends of the porous substrate, at the end portions on the surface on the opposite side to the gas feed channels, silicon carbide (Six) powder (average particle size 0.5 '0 microns, produced by Show Dunk Kabushiki Couch) was dispersed densely to a thickness of 0.1 mm, which was heated by a hot pressure bonding tool made of aluminum to 330C, whereat it was pressure bonded under a planar pressure of 20 kg/cm2 for 5 minutes.
The product was taken out from the tool, and its surface was observed. As a result, Six was found to be secured on the end surfaces through fusion of PEA
copolymer, and the surfaces subjected to this treat-mint exhibited nettability with respect to electrolytes such as phosphoric acid. Thus, end portion seals with reliability could be formed.
Example 11 At the end portions on the surface opposite to the reaction gas feed channels of the thermally fused portions of PEA copolymer formed on the ends of the porous substrate similarly as in Example 10, a mixture of 100 parts by weight of Six and 20 parts by weight of PEA copolymer powder (Teflon MY 10, produced by Mets Fluorochemical Co., Ltd.) was dispersed to a thickness of 0.2 mm and pressure bonded similarly as in Example 10. The face thus obtained exhibited nettability with respect to an electrolyte.
Example 12 At the end portions on the surface opposite to the reaction gas feed channels of the thermally fused portions of PEA copolymer formed on the ends of the porous substrate similarly as in Example 10, a paste-like mixture prepared by kneading 100 parts by weight of Sick 15 parts by weight of the PEA copolymer powder, 500 parts by weight of Dillon So (produced by Sue Kinesic Cage Co., Ltd.), which was a fluoride type dispersing medium, and 4 parts by weight of Difloil #100 (produced by Osaka Kinesic Cage Co., Ltd.) was dispersed to a thickness of 0.2 mm and pressure bonded similarly as in Example 10.
The hot pressure bonded faces at the ends of thy substrate thus obtained also exhibited wettabilit~ wit respect to an electrolyte.
Example 13 A porous plate substrate of thin graphite fibers comprising a carbon paper with a size of 70~ mm x 700 mm and a thickness of 0.5 mm (E-715, trade aye, produced by Query Kagaku Cage Co., Ltd.) was fitted at the end portions to widths each of 20 mm with a film of a tetrafluoroethylene-perfluoroalkyl vinyl ether copolymer (PEA 500 LO, trade me produced by Mets Fluorocnemi-eel Co., Ltd.) with a thickness of 0.13 mm which had been molded in a shape substantially corresponding to the end portion by softening in a mold heated at 220 -15 230C.
Then, the mold surface of the hot pressure bonding tool was covered with an aluminum foil, and the above porous substrate was placed in a mold previously coated at the necessary portions with a fluoride wax (Difloil #100, Trudy, produced by Osaka Kinesic Kiwi Co., Ltd.) and subjected to hot pressure bonding by heating at a temperature of 350 - 370C under a load of a planar pressure of 20 Kim for about 30 minutes, annealing at 80 - 90C for about one hour, and removal from the mold to complete the end portion swilling Having thus formed the thermally fused portions of PEA copolymer at the ends of the porous substrate, at the end portions on the surface on the opposite side to the gas feed channels, silicon carbide powder (average particle size 0.5 micron, produced by Show Dunk Co., Lid was dispersed similarly as in Example 10, and heated by a hot pressure bonding tool made of aluminum to 3303C, whereat it was pressure bonded under a planar pressure of 20 kg/cm for 5 minutes.
lo in this case, the end portion surface treated exhibited wetta~ility with respect to an electrolyte I
., thus evidencing formation of an end portion seal wit.
reliability.
In the above Examples 10 through 13, description has been set forth by referring particularly to tune case of hot pressure bonding with silicon carbide (Six).
Alternatively, when other substances as described above, namely titanium carbide, tantalum carbide, tungsten - carbide, zirconium oxide, tantalum oxide or carbon powder were used, it was found that good results similarly as in the above case of silicon carbide could be obtained.
Thus, when seals are formed at the end portions of a porous electrode substrate as shown in Examples 10 -through 13, it is possible to obtain a very effective porous electrode, which can exhibit nettability with respect to an electrolyte, thus being capable of retaining an electrolyte without giving rise to leakage of reaction gases and without causing breakage or other troubles.
Regarding the commercially available fluoride oils or fluoride solvents used in these Examples, first the trade name Difloil of Osaka Kinesic Cage Co., Ltd. is generally a polymer of trifluorochloroethylene ( F ) of a low polymerization degree, and exhibits an oily to waxy state depending on -the polymerization degree.
~ifloil #100 is a wax having a polymerization degree corresponding Jo a number average molecular weight of 1300. Flurried of Symptom Al Co., Ltd. is a fluorocarbon type surfactant. Dillon So is a difluoro-type wax.
Freon of Mets Fluorochemical Co., Ltd. it the general name for fluoride compounds having 1 to 4 carbon atoms to which fluoride atoms are bonded, as is jell known in the art. Monica them, Freon 113 has a molecular formula of CCl2-CClF2 and is frequently used because of its relatively high boiling point ~47.6C) and also its high volatility.
:'`
POROUS GAS DIFFUSION ELECTRODE AND
METHOD OF PRODUCT IN TOE SUE
BACKGROUND OF THE INVENTION
ethnical Field of the Invention This invention relates to a porous was diffusion electrode and a method of preparing the same and Gore particularly to a porous gas diffusion electrode provided with end portion seals constituting an electricity generating element which can ye used ion air-metal cells and fuel cells, be easily laminated, and used with high reliability and also to a method of producing the same.
Technical Background of the Invention and its Problems Air-metal toe cells or hydro~Jen-air (oxygen) fuel cells are required to have electrodes for ionization of was as their electromotive mechanisms. The gas Defoe-soon electrode, in which a was having no electroconduc-tivity participates continuously in electromotive reaction, em toys a porous plate substrate and is so constituted that one surface of the substrate is brought into contact with an electrolyte, and the gas Lyon into the substrate from the other surface is permitted to participate in the electromotive reaction within the substrate. In general, for feeding a reaction was, reaction gas feed channels are provided on the substrate itself/ or the substrate it used so as to be contacted with another element having reaction was feed channels.
In these cell systems, each unit cell outputs a voltage of at most 0.5 to 1.5 V, end hence a considerable number of unit cells are required to be laminated and provided for practical use. Turing lar.lination,unit cells are laminated in such a manner that the reaction was feed channels provided on one substrate itself or provided in contact with the substrate during use under lamination are in a direction -to cross over other was feed channels provided avow or bullet ccordinqly, it 'I
is necessary to treat the end portions on the side faces parallel to the respective gas feed channels so that one reaction was, for example, h~droyen was, flowing through one reaction was channel and another was, for example, air, flowing through another gas feed channel above or under said channel will not become mixed with each other. At the same tire, it is also necessary to treat the end portions so as to maintain electrical insulation even when compressed mechanically strongly by lamination of a large number of units.
In order to prevent mixing of different vases at the end portions of the substrate parallel to was feed channels and to ensure electrical insulation at the end portions, a method in which the end portions are coated with synthetic resins and a method in which the are impregnated with a dispersion of a tetrafluoro-ethylene copolymer have been proposed. However, none of these methods have been successful in obtaining satisfactory results.
SEYMOUR OF THE INVENTION
Accordingly, an object of the present invention is to provide a porous gas diffusion electrode for use in an air-metal cell or a hydro~en-air loden cell comprising an electroconductive porous substrate, which has itself on one surface thereof reaction gas feed channels or is to be used with one surface in contact with reaction was feed channels during usage, the electrode briny capable ox positively shielding the gas streams a-t the end portions parallel to the react lion was feed channels end maintaining electrical insulation. Another object of the invention is to provide a method of preparing such an electrode.
In accordance of the present invention, there is provided a porous was diffusion electrode comprising an electroconductive porous substrate, which has itself on one surface thereof reaction gas feed channels or is to be used with one surface in contact with reaction I
gas feed channels during use, and which comprises was impermeable and electrical insulating seals formed of a tetrafluoroethylene-perfluoroalkyl vinyl ether copolymer (hereinafter sometimes referred to as PEA
copolymer) provided on the substrate at least at both end portions parallel to said reaction gas feed channels.
The present invention also provides a method of preparing such a porous gas diffusion electrode, itch method comprises applying a tetrafluoroethylene-perfluoroalk~71 vinyl ether copolymer on the substrate at least at the end portions parallel to the reaction gas feed channels and then subjecting the substrate coated with the copolymer to hot pressure bonding by means of a pressure bonding tool jade of a metal pro-piously coated with a fluoride oil to form gas impermeable and electrically insulating seals comprise in said copolymer.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 is a perspective view of an electricity generating element including a porous gas diffusion electrode having formed seals at the end portions according to the resent invention;
FIG. 2 through 4 are schematic perspective views : respectively of the states under hot pressure bonding in a mold cavity according to the method of the present invention, wherein FIG. 2 shows the case of use of powdery or granular coupler, FIG. 3 the case of use of film copolymer, and FIG. 4 the case of use of powdery or granular copolymer and film copolymer; and FIG. 5 is a schematic illustration of the state under hot pressure bonding of a substance wettable with an electrolyte and stable thermally and chemically with respect to the electrolyte, which is further applied on the fused portion of PEA copol~f~mer.
DETAILED DESCRIPTION OF THE INVENTION
In on embodiment of the present invention as shown in FIG. 1, the electric power generating element I
comprises, in the order from above, an electrode 1 provided with reaction gas weed channels I, an electron lute layer 2, a thin electrode 3 and a laminated element provided with reaction gas feed channels 6.
The several reaction was feed channels 5 provided in the electrode 1, and the reaction gas feed channels 6 provided in the laminated element 4 are perpendicular - to each other.
- For both of the electrodes 1 and 3, porous sup-striates with a porosity of 60 to 70 which are plate shaved an are electron conductive are used. For eagle porous plates prepared by forming sistered nickel or graphite fibers into paper and then heat treating, the same can be used. The latter is suitable in a fuel cell in which a concentrated acid liquid such as gone.
phosphoric acid is used as the electrolyte.
In the present invention, at the end portions of such electrodes 1 and 3, gas impermeable, electrically insulating seals are provided. As shown in FIG. 1, in the electrode 1 provided with the reaction gas feed channels 5, these seals are provided at the end portions 7, 7 in parallel to the reaction was feed channels, while in the thin electrode 3, the are provided at the end portions 8, 8 in parallel to the reaction gas feed channels 6 provided in the laminated element I in contact with the thin electrode upon lamination. In the thin electrode 3, it is also possible to provide seals at other orations such as the end portions crossly over the channels 6, but it is necessary to provide the seals at least at the end portions 8, 8 in parallel to the channels 6.
For formation of the aroused seal, it is necessary to use a material which is capable of sealing the fine pores in the end portions to prevent passage or leak of reaction gases therethro~h and also main-lain electrical insulation in spite ox the mechanical pressure during lamination, end which has excellent . , I
chemical resistance so as to withstand hick temperature actions with the use of a concentrated acidic electron lyre and is thermally stable at temperatures in excess of 250C, even at a temperature of 350C for a short period of time. The material must also have heat-sealable property. As such a material, a tetrafluoro-ethyl-perfluoroalkylvinylether copolymer is used.
Tetrafluoroethylene has the molecular formula of CF2=CF2, as is well known in the art, and perfluoroalkyl vinyl ether the formula of SHAKER, wherein R represents a perfluoroalkyl group having ordinarily 2 to 4, preferab-lye 3, carbon atoms, of which the hydrogen atoms on the alkyd group are all substituted with fluorine atoms. The content of tetrafluoroethylene in this copolymer are with-in the range of from about 96 to 97 by weight.
This copolymer is commercially available in the form of powder, granules, film and emulsion. These forms can be used either singly or in any desired combination. For example, the above copolymers in the form of powder or granules can be dispensed on the surface at the end portions and then subjected to pressurization into the porous substrate by application of heat and pressure, or a film of the above copolymer can be covered all over the end portions, namely in U-shape, and then subjected to application of heat and pressure thereon to cause the film to be closely contacted by the porous substrate ends, thereby forming seals.
It is also possible to disperse the above Capella-men in the form of powder or granule on the surfaces of the end portions, then cover the surfaces with a film of the above copolymer, and apply heat and pressure to the film to form seals. alternatively, the surfaces of the end portions can be coated with the copolymer in state of emulsion, and then heat and pressure applied thereto, or further a film of the copolymer can be placed thereon, tush step is followed by a similar :
application of heat and pressure to form seals.
The method of forming the end portion seals on such porous gas diffusion electrodes 1 and 3 isle nudge - be described in treater detail. The above mentioned copolymer in the form of powder or granules is mixed with a suitable solvent such as one of fluoride type and stirred at room temperature to 40C to prepare a mixed agent. This mixed agent is applied on the surfaces of the end portions of the porous substrate constituting the electrode and dried in air to cause the powdery or granular copolymer to be dispersed evenly throughout the surfaces of the end portions, Its amount is such that there will be a rise of the sealant of about 0.1 to 0.3 em after hot pressure bonding and air drying. Then, the substrate is placed within a female mold of a pressure bonding tool made, of a metal such as a mold cavity coated previously with a mold releasing agent comprising a fluoride oil, and a male mold is placed against the surfaces of the end portions having the above copolymer dispersed therein. Then pressure bonding is carried out while heating the whole assembly to a temperature not higher than 380C, preferably 340 to 350C under pressurize-lion ox about 20 to 40 kg/cm2 in terms of planar pressure.
As the fluoride oil, co~ercially available fluoride wax may be used as it is, or this may be further idea with a fluoride solvent under stirring before use. What is important here is that at least 3Q the necessary portions on the surface ox the pressure bonding tool, namely, the portions to be contacted by the portions on which the above copolymer is dispersed or deposited, should previously be coated with a fluoride oil as a told releasing agent. it is also 'I 35 important to control the temperature to a value not higher than 380C. Since the above copolymer has good heat-sealable property with respect to a petal, told ;
release can be easily carried out with tune use of a fluoride oil as the mold releasing agent. On tune other hand, the above powclerv or granular copolYmer will begin to generate bubbles at a temperature in excess of 380C, whereby uniform formation of seals is rendered impossible. In practice, heating is carried out at a temperature of 340 - 330C under the planar pressure mentioned above for 15 to 30 minutes, and then annealing is conducted at 80 to 90C for about one hour, followed by removal of the sealed product from the mold.
This method is indicated in FIG. 2, in itch a powdery of granular copol~tmer 11 is disperse on the surfaces of a porous substrate 10 for formation of an electrode, at the end portion thereof. On the other hand, the mold is previously coated with a mold releasing agent comprising a fluoride oil at the corner portion of a female mold 12 and the pressure bonded face of a male mold 13, namely at the sites to be contacted with the surface where the above copolymer is dispersed. As illustrated in the drooling, the porous substrate 10, on which the above copolymer 11 is dispersed in an amount such that it Lyle be raised to about 0.1 to 0.3 mm after air clarion, is placed within the female mold 12 previousltl/ coated with the fluoride oil motel releasing agent, and then hot pressure bonding is carried out by means of the male mold similarly coated with the mold releasing agent 14 by pressurization from upward and downward directions A and B.
In the case where the above calmer is used in the form of a film, oration of the seal is possible in substantially the save manner. More specie ficall~r, as shown in FIG. 3, the above calmer 15 in the form of a film with a thickness of about 0.1 to 0.2 mm is placed as a cover on the surface of thy end portion of the porous substrate 10 with a Ushered cross-section, and the covered substrate is placed within the female mold 12 coated previously with a fluoride oil mold releasing agent I after which hot pressure bonding is carried out by pressurization from both upward and downward directions. Also, in this case, the heating temperature must not exceed 380C, and a good seal portion can be for~ecl in practice by heating to 340 to 380C under pressurize-lion of a planar pressure of about 20 to 40 k~/cm2 for 15 to 30 minutes and then performing annealing at a temperature of 80 - 90C for about one hour, thereby pressurizing the above coupler into the porous substrate.
Referring no to FIG. I, here the powdery or granular copolymer 11 is dispersed first similarly as described above on the surface of the end portions of the porous substrate 10, and further the cooolvmer 15 in form of a film with a thickness as specified above is placed there over as a cover before placement of the substrate within a female told 12 coated previously at the necessary portion With a fluoride oil 14. Then hot pressure bonding is carried out under the save pressure and temperature conditions as described above. It is also possible to disperse first the powdery or granular polymer, which is then subjected to hot pressure bonding to be pressurized into the porous substrate, and then to place a film copolymer as a cover over the substrate and carry out hot pressure bonding again.
In addition, a copolymer in the state of an emulsion can be applied on the surface of a porous substrate an dried, after josh it is subjected to hot pressure bonding in a motel to be pressurized into the porous substrate. Alternatively, as described above, aster coating an drying, a film copolymer can be place as a cover over the substrate, and there-after hot pressure bonding can be carried out. Such I
g a copolymer in the state of an emulsion can ye pry' by, for example, adding 100 parts by weight of -Atari and 1 to 5 parts by weight of a non ionic surfactant to 20 to 60 parts by weight of the powdery or granular copolymer and vigorously stirring the mixture.
As described above, PEA copolymer is commercially available in various forms such as powder, granules, film, emulsion, etc., and can be used in any desired form. When PEA copolymer in the form of a film is employed, the copolymer can be previously formed in the shape of the letter U in cross-section so as to correspond to the shape of the aforesaid end portion, and the formed film is placed over the entire end portion, which step is followed by application of heat and pressure to obtain close contact of the film against the end portions of the porous substrate to -form seals. By this process, improvement ox yield can be brought about.
Alternatively, it is also possible to form seals by dispersing or applying the aforesaid copolymer in the form of powder, granules or emulsion on the surface of the end portions before placing the above copolymer molded in a film there over, and then applying heat and pressure to the film.
More specifically, the above copolymer in the form of flat film is relatively hard, and therefore it is not easily placed over the end portion. Accord-tingly, the film employed is previously heated to 20Q
to 230C and molded by means of a working tool into a U-shape in cro~s-section corresponding to the end portion. PEA copolymer in the form of a molded film is placed as a cover over the end portion of a porous substrate. The cowered substrate is then placed in a female mold of a pressure bonding tool ox a metal sun as a mold cavity made of aluminum or an aluminum alloy having a smooth surface coated previously with a mold releasing agent comprising a fluoride oil, and a male ~2~L81~1 mold coated similarly on the surface of the end portion with a mold releasing agent is pressed against the covered substrate. Finally, this step is foolhardy by heating under pressurization at a temperature within the range of from 340 to 350C for 15 to 30 minutes to accomplish hot pressure bonding.
As the fluoride oil, commercially available fluoride wax may be used as it is, or a mixture of such a wax can be further mixed with a fluoride solvent under stirring before use. What is important here is to employ a working -tool having a smooth surface made of aluminum or an aluminum alloy, in view of the fact that the above copolymer having a generally good heat-seal property with respect to metals was found by experiment to be difficult to attached by melting to aluminum or an aluminum alloy, and to coat previously, the necessary portion of the worming tool, namely, the portion contacted by the covered portion of the above copolymer,with a mold releasing agent. It is also important not to elevate the temperature above 380C.
The working tool for pressure bonding made of aluminum or an aluminum alloy is not limited to those made wholly of aluminum metal or aluminum alloy, but it is also possible to use favorably one which is coated on the surface corresponding to the bonded portion with â
foil of aluminum metal or an aluminum alloy.
Further, in the present invention, after formation okay' the hot pressure bonded portion of PEA copolymer at the end portion of a porous substrate, a substance that -is wettable With an electrolyte and is thermally and chemically stable with respect to an electrolyte can be provided by not pressure bondincJ to Norm a gas , impermeable and electrically insulating seal formed of PEA copolymer and the aforesaid substance at the end portion, whereby it is possible to obtain an electrode which is wettable with an electrolyte between the electrodes, is capable ox retaining an ample amount of the electrolyte in the electrolyte layer and further has an end portion seal with reliability. examples of the substance used here are silicon carbide, titanium carbide, tantalum carbide, tungsten carbide, zirconium oxide, tantalum oxide, and carbon powder.
These may be used either singly or as any combination thereof. Any of these substances exhibits good nettability with respect to an electrolyte and is chemically stable without being corroded by the electrolyte. It is also stable at high temperatures of about 200C or higher at which the fuel cell employing the electorate operates. This substance is ordinarily employed in the form of powder or granules.
The place where this substance is pressure bonded under heating may be the whole fused portion of PEA
copolymer formed in the shape of U in cross-section ; on the end portion of the substrate as described above, but the substance is applied by hot pressure bonding on the fused portion of PEA copolymer at least on the side opposite to the surface having the aforesaid reaction gas feed channels or opposite to the face to be in contact with the reaction gas feed channels when used under lamination.
- US In practicing hot pressure bonding of such a substance, as shown in FIG. 5, on the surface of the fused portion 18 formed at the end portion of the porous substrate 17 having reaction gas feed channels on one surface, at least on the face opposite to the face having the reaction gas feed channels 16, a substance 19 wettable with an electrolyte and thermally and chemically stable with respect to the electrolyte is dispersed densely to a thickness of about 0.05 to 0.3 mm, which is then subjected to hot pressure bond-in by means ox a hot pressure bonding tool made of metal such as aluminum as shown in FIX. 2 while being heated to a temperature ox 300 to 370C under a planar ,.
I"
Jo pressure similarly as described above.
The substance wettable with an electrolyte and thermally and chemically stable with respect to toe electrolyte as mentioned above may be used solely, but it can be also used in the form of a mixture with the above PEA copolymer or in the form of a paste e mixture prepared by mixing the three components of the substance, the above PEA copolymer and a fluoride type dispersing medium. The proportions are preferably 3 10 to 40 parts by weight of PEA copolymer powder per 100 parts by weight of the above substance in the former case, while the proportions are preferably 3 to 40 parts by weight of PEA copolymer powder and 150 to 600 parts by weight of a fluoride type dispersing medium per 100 parts by weight of the above substance in the latter case. The conditions during hot pressure bonding such as the temperature are substantially the same as in the case where the above substance along is used.
Thus, the porous gas diffusion electrode obtained according to the present invention by forming gas impermeable, electrically insulating seals comprising a tetrafluoroethylene-perfluoroalk~l vinyl ether copolymer at least at both end portions parallel to the reaction gas feed channels of a porous substrate not only can prevent completely leakage of reaction gas from the end portions but also will not be broken under strong pressure during lamination of electricity generating elements such as these electrodes due to its mechanical reinforcement, having also good electrical insulating property or complete prevention of semi-short circuiting at the end portions frequently occu~rinq in tune past. Also, since lamination of electricity generating elements has been simplified, toe time needed for laminating assembly thereof can be shortened to a great extent and high reliability of the lam-noted product can be maintained. In this connection, I
. .
when electricity generating elements were formed by tune use of a porous substrate subjected to treatment of the end portions with a polytetrafluoroethylene suspension, the yield was only about 2/5 as compared with the case in which the electrode of the present invention was employed, and lamination was also difficult. Thus, the present invention has also additional merits such as improvement of yield to a great extent.
If the above copolymer in the form of a flat film which is not contour able along the shape of the end portion is employed, it cannot be set well in position in the shape of the end portion, for example, a U-shaped cross-section, whereby the yield after hot pressure bonding will become only 50 to 60 I. By permitting the above copolymer film to substantially coincide in shape with the end portion, for example, molding the film to have a U-shaped cross-section, and carrying out hot pressure bonding with the molded film covering the end portion, the yield can be improved to 30 to 90 %.
Further, by making the surface of the working tool for hot pressure bonding of smooth aluminum or aluminum alloy, no melt adhesion of the copolymer to the mold cavity will occur, whereby a yield close to 100 % can be attained.
; 25 Also, by further applying a substance wettable with an electrolyte and thermally, chemically stable with respect to the electrolyte by hot pressure bonding on the surface of the fused portion obtained by hot pressure bonding of PEA copolymer at both end portions parallel to the reaction gas feed channels on a porous plate substrate, at least on the surface of the fused portion on the side opposite to the face having the reaction gas feed channels or on the side oppose e to the face to be contacted with the reaction gas feed channels when laminated, the aforesaid suffuse can ` exhibit nettability with an electrolyte such as pros-phonic acid, whereby a sufficient amount of electrolyte I, .., can be held in the electrolyte layer between electrodes, and the leak of reaction gas can be prevented. The above substance, and toe fused portion will not be peeled off, and of course the seal can withstand the strong pressure during lamination without incurring breakage thereof to maintain its good electrical insulation, thus providing a porous electrode having end portion seals which are reliable.
Example 1 A mixture of 192 g of a tetrafluoroethyleneperfluoro-alkyd vinyl ether copolymer (Teflon MP-20, trade mark, produced by Mets Fluorochemical Co., Ltd.) and 128 g of a fluoride type solvent (Flurried FC 721, trade mark, Symptom EM Co., Ltd.) was stirred at room temperature for 30 minutes to prepare a mixed agent for coating.
Then, a porous plate substrate made of thin graphite fibers comprising a carbon paper with a size of 700 my x 700 mm and a thickness of 0.5 mm (E-715, trade mark, produced by Zaire Kagaku Co., Ltd.) was coated at both end portions with the above mixed agent to widths each of 20 mm and left to stand for air drying to cause the above copolymer to be dispersed at said end portions.
Separately, a mold as shown in the drawings was previously coated at the necessary portions with a fluorine wax ; (Difloil #100, trade mark, produced by Osaka Kinesic Kiwi Co., Ltd.), and the porous substrate as prepared above was placed within the mold, and heated at a temperature of 340 to 370C under a load of a planar pressure of 20 kg/cm2 for about 15 minutes, after which annealing was carried out at 80 to 90C for about one hour.
When the mold was removed, and the product was left to stand for air drying, the above copolymer was found to be pressurized into the substrate and attached with a rise of about 0.1 mm.
The sealed portion thus formed was uniform at the end face without any leakage of gas whatsoever, was mechanically strengthened after lamination, and had good electrical insulating property.
Example 2 A mixture of 192 g of a tetrafluoroethyleneperfluoro-alkyd vinyl ether copolymer (Teflon MP-10, trade mark, produced by Mets Fluorochemical Co., Ltd.) and 128 g of a fluoride type solvent (Dillon Solvent So, trade mark, produced by Osaka Kinesic Cage Co., Ltd.) was stirred under heating at 45 to ~0C for 30 minutes to prepare a mixed agent for coating.
Then, by using as the substrate a carbon paper with a size of 700 mm x 700 mm and a thickness of 2 mm (E-750, trade mark, produced by Query Kagaku Jo., Ltd.3 prepared by she~t-making of graphite fibers, the substrate was coated at both end portions with the above mixed agent to widths Mach of 20 mm and left to stand for air drying to cause the above copolymer to be dispersed at the end portions.
Separately, with the use of a mold releasing agent prepared by homogenization of a mixture of 120 g of a fluoride wax (Difloil #100, trade mark, produced by Osaka Kinesic Kiwi Co., Ltd.) and 180 g of a fluoride solvent (Freon 113, trade mark, produced by Mets Fluorocnemical Co., to by stirring at 45 to 50C for 30 minutes, a mold was coated at necessary portions with the mold releasing agent The above porous substrate was placed in or I, the mold and subjected to hot pressure bonding similarly as described in Example l. The above copolymer was found to be pressurized into the substrate and attached after air drying with a rise of about 0.3 mm on the surface. A sealed portion with excellent gas impermeability and electrical insulation was formed, whereby leakage of gas could be completely prevented.
Example 3 A porous plate substrate of thin graphite fibers comprising a carbon paper with a size of 700 mm x 700 mm and a thickness of 0.5 mm (E-715, trade mark, produced by Query ~agaku Cage Co., Ltd.) was coated at the end portions with a film of a tetrafluoroethylene-perfluoro-alkyl vinyl ether copolymer (PEA
500 LO, trade mark, produced by Mets Fluorochemical Co., Ltd.) with a width of 20 mm and a thickness of 0.13 mm in the shape of U.
Then, the above porous substrate was placed in a mold previously coated at the necessary portions with a fluoride wax (Difloil #100, trade mark, produced by Osaka Kinesic Cage Co., Ltd.), and subjected to hot pressure bonding by heating at a temperature of 350 to 370C under a load of a planar pressure of 20 kg/cm or about 30 minutes, annealing at 80 to 90C for about one hour, and removal from the mold to complete the end portion sealing. The end portion seal thus obtained was found to be uniform at the end surface, and there was no gas leakage whatsoever from this portion.
Example _ A mixture of lg2 g of a powdery tetrafluoroethylene-perfluoroalkyl vinyl ether copolymer (Teflon HP-20, trade mar, produced by Mets Fluorochemical Co., Ltd.) and 128 g of a fluoride .......
I'.. .' I
.
~2~B~
type solvent (Flurried FC 721, trade mark, Symptom I co ., ~td.3 aye stirred at room temperature for 30 minutes to prepare a mixed agent for coating.
Then, a porous plate substrate made of thin graphite fibers which was a carbon paper with a size of 700 mm x 700 mm and a thickness of 2 mm (E-750, trade mark, produced by Query Kagaku Co., Ltd.) was coated at both end portions with the above mixed agent to widths each of 20 mm and left to stand for air drying, which step was followed by further coating with a film of a twitter-fluoroethylene-perfluoroalkyl vinyl ether copolymer (PEA 500 LO, trade mark, produced by Mets Fluorochemical Co., Ltd.) with a width of 30 mm and a thickness ox 0.13 mm in the shape of U.
Separately, a fluoride oil was prepared by mixing 120 g of a fluoride wax (Difloil ~100, trade mark, produced by Osaka Kinesic Cage Co., Ltd.) and 180 g of a fluoride solvent Freon 113, trade mark produced by Mets Fluorochemical Co., Ltd.) under stir-ring at 45 to 50C for I minutes. The above porous substrate have in the powdery and film copolymers dispersed or coated at the end portions as described above was placed in a mold, which had been previously coaxed with thy fluoride oil, and subjected -to hot pressure bonding under the same conditions as in Example 3 to form end portion seals.
From the end portion seals thus formed, there was no gas leakage whatsoever, the end surface being smooth. Particularly no deterioration was detected in a cell prepared ho lamination of the electricity generating elements containing the electrodes obtained by the use of this seal after operation at a high -temperature for a long time. The result was also similar with respect to electrical insulation.
aye Example 5 To 40 parts by weight of a tetrafluoroethylene-perfluoroalkyl vinyl ether copolymer (Teflon MP-20, trade mark, produced by Mets Fluorochemical Co., Ltd.) were added 100 parts by weight of water and 3 parts of a non ionic surfactant (Briton X-100, trade mark, produced by Room Hays Japan Co,, Ltd.), and the mixture was vigorously stirred for dispersion of the above copolymer thereby to prepare an emulsion thereof.
As the next step, a porous plate substrate made of thin graphite fibers comprising a carbon paper with a size of 700 mm x 700 mm and a thickness of 0.5 mm (E-715, trade mark, produced by Query Kagaku Co., Ltd.) was coated at both end portions with the above emulsion to widths of 20 mm and dried.
Then/ hot pressure bonding was carried out in a mold coated with a fluoride oil similarly as in Example 1. As a result, seal portions having good electrical insulation without gas leakage from the end surfaces were similarly obtained.
Example 6 An emulsion of the tetrafluoroethylene-perfluoro-alkyd vinyl ether copolymer was prepared in the same manner as in Example 5, and the thin carbon paper was coated with this emulsion and dried. This was further coated with a film of tetrafluoroethylene-perfluoro-alkyd vinyl ether copolymer (PEA 500 LO, trade -ye, produced by Mets Fluorochemical Co., Ltd.) with a thickness of 0.13 mm in shape of U.
Following thereafter the same procedure as in Example 1, hot pressure bonding was carried out under the same conditions in a mold coated with the fluoride oil. As a result, sealed portions having excellent gas impermeability and electrical insulation property were formed.
Example 7 _ A porous plate substrate of thin graphite fibers comprising a carbon paper with a size of 700 mm 700 mm 25 and a thickness of 0.5 mm (E-715, trade aye, produced by Query Kagaku Cage Cowl Ltd.) was provided at the end portions to widths each of 20 mm with a film of a tetrafluoroethylene-perfluoroalkyl vinyl ether copolymer (PEA 500 LO, trade-n~ffl~, produced by Mets Flyer-chemical Co., Ltd.) with a thickness ox 0.13 em which had been molded in the shape substantially corresponding to the end portion by softening in a mold heated at 220 - 230C.
Then, the mold surface ox the hot pressure bond-in tool was covered with an aluminum foil, and the above porous substrate was placed in a mold previously coated at the necessary portions with a fluoride way (Difloil #100, trade mark, produced by Osaka Xinzoku Cage Coy, Ltd.), and subjected Jo hot pressure bonding by heating at a temperature of 350 - 370C under a load of a planar pressure of 20 kg/cm2 for about 30 minutes, annealing at 80 - 90C for about one hour, and removal from the mold to complete the end portion sealing. The end portion seal thus obtained was found to be uniform at the end surface without any gas leakage.
Example 8 mixture of 192 g of a powdery tetrafluoroethylene-perfluoroalkyl vinyl ether copolymer (Teflon HP-20, trade mark, produced by Mets Fluorochemical Co., Ltd.) and 128 g of a fluoride type solvent (Flurried FC 721, trade mark, Symptom EM Co., ; Ltd.) was stirred at room temperature for 30 minutes to prepare a mixed agent for coating.
Then, by using as the porous plate substrate a carbon paper with a size of 700 mm x 700 mm and a thickness of 2 mm (E-750, trade mark, produced by Query Kagaku Co., Ltd.) prepared by sheet making of graphite fibers, the substrate was coated at end portions with the above mixed agent to widths of 20 mm and dried in air end further provided with a film of a tetrafluoroethyl-ene-perfluoroalkyl vinyl ether copolymer (PEA 50Q LO, trade mark, produced by Mets Fluorochemical Co., Ltd.) with a thickness of 0.13 mm which had previously been formed into a U-shape similarly as described in Example 7.
Separately, a fluoride oil was prepared by mixing 120 g of a fluoride wax (~ifloil #100, trade mark, produced by Osaka Kinesic Cage) and 180 g of a fluorine solvent Freon 113, trade mark, produced by it's Fluorochemical Co., Ltd.) under stirring I
at 45 - 50C for 30 minutes. The above described porous substrate having the powdery and film copolymers dispersed or coated at the end portions as described above was placed in a mold, which had been previously coaxed with the fluoride oil, and subjected to hot pressure bonding under the same conditions as in Example 7 to form end portion seals.
From the end portion seals thus formed, there was no gas leakage whatsoever, the end surface being smooth. Particularly, no deterioration way detected in a cell prepared by lamination of the electricity generating elements containing the electrodes obtained by the use of this seal after operation at a high temperature for a long time. The result was also similar with respect ; to electrical insulation.
Example 9 .
To 40 parts by weight of a tetrafluoroethylene-perfluoroalk.yl vinyl ether copolymer (Teflon MP-~0, trade mark, produced by Mets Fluorochemical Co., Ltd.) were added 100 parts by weight of water and 3 parts of a non ionic surfactant Briton X-100, trade mark, produced by Room & Hays Japan Co., Ltd.), and the mixture was vigorously stirred for dispersion of the above Capella-men, to prepare an emulsion thereof.
As the next step r a porous plate substrate made of thin graphite fibers comprising a carbon paper with a size of 700 mm x 700 mm and a thickness of 0.5 mm (E-715, trade mark, produced by Query Kagaku Co., Ltd.) was coated at both end portions with the above emulsion to widths each of I mm and dried.
Subsequently, a film of a tetrafluoroethylene-perfluoroalkyl vinyl ether copolymer (PEA 500 LO, trade mark, produced by Mets ,,,,'~ ~72_ Fluorochemical Co., Ltd.1 with a thickness of 0.13 em was formed into a U-shape similarly as described in Example 7, and the end portions of the above coated substrate were inserted whereinto.
Then, hot pressure bonding was carried out in a mold formed of Solomon, which is an aluminum alloy, coated with a fluoride oil similarly as in Example 7 under the same conditions.
As a result, seal portions of excellent gas impermeability and electrical insulation property were obtained.
Example 10 A mixture of 192 g of a tetrafluoroethylene-perfluoro-alkyd vinyl ether copolymer (PEA copolymer) (Teflon MP-20, trade mark, produced by Mets Fluorochemical Co., Ltd.) and 12~ g of a fluoride type solvent (Flurried FC 721, trade mark, Symptom EM Co., Ltd.) was stirred at room temperature for 30 minutes to prepare a mixed agent for coating.
Then, a porous plate substrate made of thin graphite fibers comprising a carbon paper with a size of 700 mm x 700 mm and a thickness of 0.5 mm EYE, trade mark, produced by Query Kagaku Co., Ltd.) was coated at both end portions with the above mixed agent to widths lack of 20 mm and left to stand for air drying to cause the above copolymer to be dispersed at said end portions.
Separately, a mold as shown in the drawings was pry-piously coated at the necessary portions with a fluoride wax (Difloil #100, trade mark, produced by Osaka Kinesic Cage Co., Ltd.), and the porous substrate a prepared above was placed within the mold and heated at a temperature of 34Q - 370~C under a load of a planar pressure of 20 kg/cm2 for about 15 minutes, which step . ..
,, I.
I
aye was followed by annealing at 80 - 90C for about one hour. r~rnen the mold was removed, and the product was left to stand for air drying, the above copolymer was found to be pressurized into the substrate and the thermally fused portion of PEA copolymer formed, being attached with a rise of about 0.1 mm.
Having thus formed the thermally fused portions of PEA copolymer at the ends of the porous substrate, at the end portions on the surface on the opposite side to the gas feed channels, silicon carbide (Six) powder (average particle size 0.5 '0 microns, produced by Show Dunk Kabushiki Couch) was dispersed densely to a thickness of 0.1 mm, which was heated by a hot pressure bonding tool made of aluminum to 330C, whereat it was pressure bonded under a planar pressure of 20 kg/cm2 for 5 minutes.
The product was taken out from the tool, and its surface was observed. As a result, Six was found to be secured on the end surfaces through fusion of PEA
copolymer, and the surfaces subjected to this treat-mint exhibited nettability with respect to electrolytes such as phosphoric acid. Thus, end portion seals with reliability could be formed.
Example 11 At the end portions on the surface opposite to the reaction gas feed channels of the thermally fused portions of PEA copolymer formed on the ends of the porous substrate similarly as in Example 10, a mixture of 100 parts by weight of Six and 20 parts by weight of PEA copolymer powder (Teflon MY 10, produced by Mets Fluorochemical Co., Ltd.) was dispersed to a thickness of 0.2 mm and pressure bonded similarly as in Example 10. The face thus obtained exhibited nettability with respect to an electrolyte.
Example 12 At the end portions on the surface opposite to the reaction gas feed channels of the thermally fused portions of PEA copolymer formed on the ends of the porous substrate similarly as in Example 10, a paste-like mixture prepared by kneading 100 parts by weight of Sick 15 parts by weight of the PEA copolymer powder, 500 parts by weight of Dillon So (produced by Sue Kinesic Cage Co., Ltd.), which was a fluoride type dispersing medium, and 4 parts by weight of Difloil #100 (produced by Osaka Kinesic Cage Co., Ltd.) was dispersed to a thickness of 0.2 mm and pressure bonded similarly as in Example 10.
The hot pressure bonded faces at the ends of thy substrate thus obtained also exhibited wettabilit~ wit respect to an electrolyte.
Example 13 A porous plate substrate of thin graphite fibers comprising a carbon paper with a size of 70~ mm x 700 mm and a thickness of 0.5 mm (E-715, trade aye, produced by Query Kagaku Cage Co., Ltd.) was fitted at the end portions to widths each of 20 mm with a film of a tetrafluoroethylene-perfluoroalkyl vinyl ether copolymer (PEA 500 LO, trade me produced by Mets Fluorocnemi-eel Co., Ltd.) with a thickness of 0.13 mm which had been molded in a shape substantially corresponding to the end portion by softening in a mold heated at 220 -15 230C.
Then, the mold surface of the hot pressure bonding tool was covered with an aluminum foil, and the above porous substrate was placed in a mold previously coated at the necessary portions with a fluoride wax (Difloil #100, Trudy, produced by Osaka Kinesic Kiwi Co., Ltd.) and subjected to hot pressure bonding by heating at a temperature of 350 - 370C under a load of a planar pressure of 20 Kim for about 30 minutes, annealing at 80 - 90C for about one hour, and removal from the mold to complete the end portion swilling Having thus formed the thermally fused portions of PEA copolymer at the ends of the porous substrate, at the end portions on the surface on the opposite side to the gas feed channels, silicon carbide powder (average particle size 0.5 micron, produced by Show Dunk Co., Lid was dispersed similarly as in Example 10, and heated by a hot pressure bonding tool made of aluminum to 3303C, whereat it was pressure bonded under a planar pressure of 20 kg/cm for 5 minutes.
lo in this case, the end portion surface treated exhibited wetta~ility with respect to an electrolyte I
., thus evidencing formation of an end portion seal wit.
reliability.
In the above Examples 10 through 13, description has been set forth by referring particularly to tune case of hot pressure bonding with silicon carbide (Six).
Alternatively, when other substances as described above, namely titanium carbide, tantalum carbide, tungsten - carbide, zirconium oxide, tantalum oxide or carbon powder were used, it was found that good results similarly as in the above case of silicon carbide could be obtained.
Thus, when seals are formed at the end portions of a porous electrode substrate as shown in Examples 10 -through 13, it is possible to obtain a very effective porous electrode, which can exhibit nettability with respect to an electrolyte, thus being capable of retaining an electrolyte without giving rise to leakage of reaction gases and without causing breakage or other troubles.
Regarding the commercially available fluoride oils or fluoride solvents used in these Examples, first the trade name Difloil of Osaka Kinesic Cage Co., Ltd. is generally a polymer of trifluorochloroethylene ( F ) of a low polymerization degree, and exhibits an oily to waxy state depending on -the polymerization degree.
~ifloil #100 is a wax having a polymerization degree corresponding Jo a number average molecular weight of 1300. Flurried of Symptom Al Co., Ltd. is a fluorocarbon type surfactant. Dillon So is a difluoro-type wax.
Freon of Mets Fluorochemical Co., Ltd. it the general name for fluoride compounds having 1 to 4 carbon atoms to which fluoride atoms are bonded, as is jell known in the art. Monica them, Freon 113 has a molecular formula of CCl2-CClF2 and is frequently used because of its relatively high boiling point ~47.6C) and also its high volatility.
:'`
Claims (17)
1. A porous gas diffusion electrode constituted of an electroconductive porous substrate, which has itself on one surface reaction gas feed channels or is to be used with one surface in contact with reaction gas feed channels during use, which comprises gas impermeable and electrically insulating seals formed from a material comprising a tetrafluoroethylene-perfluoroalkyl vinyl ether copolymer (PFA copolymer) provided on the substrate at least at both end portions parallel to said reaction gas feed channels.
2. A porous electrode according to Claim 1, wherein the gas impermeable and electrically insulating seals are formed from a PFA copolymer and a substance wettable with respect to an electrolyte and thermally and chemically stable with respect to the electrolyte.
3. A porous electrode according to Claim 2, wherein the substance wettable with respect to an electrolyte and thermally and chemically stable with respect to the electrolyte is used on the substrate at least at the hot pressure bonded portion formed from the PFA copoly-mer on the face opposite to the face having the reaction gas feed channels or the face opposite to the face to be contacted with the reaction gas feed channels during use.
4. A porous electrode according to Claim 1, wherein the PFA copolymer in any of powdery, granular, film, and emulsion forms is used singly or in combination.
5. A porous electrode according to Claim 2, wherein the substance wettable with respect to an electrolyte and thermally and chemically stable with respect to the electrolyte is one or a combination of two or more of silicon carbide, titanium carbide, tantalum carbide, tungsten carbide, zirconium oxide, tantalum oxide and carbon powder.
6. A porous electrode according to Claim 2, wherein the substance wettable with respect to an electrolyte and thermally and chemically stable with respect to the electrolyte is used as a mixture with the PFA copolymer.
7. A porous electrode according to Claim 2, wherein the substance wettable with respect to an electrolyte and thermally and chemically stable with respect to the electrolyte is used as the paste-like mixture with the PFA copolymer and a fluoride type dispersing medium.
8. A method of preparing a porous gas diffusion electrode constituted of an electroconductive porous substrate, which has itself on one surface reaction gas feed channels or is to be used with one surface in contact with reaction gas feed channels during use, which comprises applying a tetrafluoroethylene-per-fluoroalkyl vinyl ether copolymer on the substrate at least at the end portions parallel to the reaction gas feed channels and then subjecting the substrate coated with the copolymer to hot pressure bonding by means of a pressure bonding tool made of a metal previously coated with a fluoride oil to form gas impermeable and electrically insulating seals.
9. A method according to Claim 8 further comprising the steps of further applying after the hot pressure bonding of the PFA copolymer a substance wettable with respect to an electrolyte and thermally and chemically stable with respect to the electrolyte and hot pressure bonding by means of a pressure bonding tool made of aluminum or its alloy to form gas impermeable and electrically insulating seals.
10. A method according to Claim 9, wherein the substance wettable with respect to an electrolyte and thermally and chemically stable with respect to the electrolyte is applied on the substrate at least at the hot pressure bonded portion formed from the PFA
copolymer on the face opposite to the face having the reaction gas feed channels or the face opposite to the face to be contacted with the reaction gas feed channels during use.
copolymer on the face opposite to the face having the reaction gas feed channels or the face opposite to the face to be contacted with the reaction gas feed channels during use.
11. A method according to Claim 8, wherein the PFA
copolymer in any of powdery, granular, film, and emul-sion forms is used singly or in combination.
copolymer in any of powdery, granular, film, and emul-sion forms is used singly or in combination.
12. A method according to Claim 11, wherein the PFA copolymer is molded by heating to correspond to the shape of the end portion of the substrate before use.
13. A method according to Claim 9, wherein the substance wettable with respect to an electrolyte and thermally and chemically stable with respect to the electrolyte is one or a combination of two or more of silicon carbide, titanium carbide, tantalum carbide, tungsten carbide, zirconium oxide, tantalum oxide and carbon powder.
14. A method according to Claim 9, wherein the substance wettable with respect to an electrolyte and thermally and chemically stable with respect to the electrolyte is used as a mixture with the PFA copolymer.
15. A method according to Claim 9, wherein the substance wettable with respect to an electrolyte and thermally and chemically stable with respect to the electrolyte is used as the paste-like mixture with the PFA copolymer and a fluorine type dispersing medium.
16. A method according to Claim 8 or Claim 9, wherein the PEA copolymer is subjected to hot pressure bonding at a temperature of 340 to 380°C.
17. A method according to Claim 9, wherein the substance wettable with respect to an electrolyte and thermally and chemically stable with respect to the electrolyte is subjected to hot pressure bonding at a temperature of 300 to 370°C.
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP80553/1983 | 1983-05-09 | ||
| JP58080553A JPH0652658B2 (en) | 1983-05-09 | 1983-05-09 | Fuel cell |
| JP198313/1983 | 1983-10-25 | ||
| JP58198313A JPS6091560A (en) | 1983-10-25 | 1983-10-25 | Manufacture of porous gas diffusion electrode |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1218111A true CA1218111A (en) | 1987-02-17 |
Family
ID=26421552
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA000453757A Expired CA1218111A (en) | 1983-05-09 | 1984-05-08 | Porous gas diffusion electrode and method of producing the same |
Country Status (4)
| Country | Link |
|---|---|
| US (1) | US4555324A (en) |
| EP (1) | EP0125595B1 (en) |
| CA (1) | CA1218111A (en) |
| DE (1) | DE3465393D1 (en) |
Families Citing this family (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA2090477A1 (en) * | 1990-08-28 | 1992-03-01 | James L. Mcguire | Method of and apparatus for introducing an impregnating fluid into a porous substrate region |
| WO1993013566A1 (en) * | 1991-12-26 | 1993-07-08 | International Fuel Cells, Inc. | Plate-shaped fuel cell component and a method of making the same |
| US5837395A (en) * | 1995-12-21 | 1998-11-17 | International Fuel Cells | Corrosion resistant fuel cell assembly |
| US5976726A (en) | 1997-05-01 | 1999-11-02 | Ballard Power Systems Inc. | Electrochemical cell with fluid distribution layer having integral sealing capability |
| DE10040282A1 (en) * | 2000-08-14 | 2002-03-07 | Robert Heggemann | fuel cell |
| DE10064462A1 (en) * | 2000-12-22 | 2002-07-18 | Mtu Friedrichshafen Gmbh | Process for the production of electrodes, components, half cells and cells for electrochemical energy converters |
| EP1654776B1 (en) * | 2003-07-14 | 2013-09-11 | Umicore AG & Co. KG | Membrane electrode assembly for use in electrochemical devices |
| US20050014056A1 (en) * | 2003-07-14 | 2005-01-20 | Umicore Ag & Co. Kg | Membrane electrode unit for electrochemical equipment |
| US20100075199A1 (en) * | 2006-12-20 | 2010-03-25 | Darling Robert M | Hydrophobic layer for a fuel cell |
| KR102364847B1 (en) | 2015-05-15 | 2022-02-18 | 삼성전자주식회사 | Metal air battery and gas diffusion layer |
Family Cites Families (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| NL136428C (en) * | 1965-09-11 | 1900-01-01 | ||
| DE2503215C2 (en) * | 1975-01-27 | 1986-08-07 | Keramchemie GmbH, 5433 Siershahn | Device for the electrolysis of hydrochloric acid |
| US4259389A (en) * | 1977-12-12 | 1981-03-31 | United Technologies Corporation | High pressure-low porosity wet seal |
| US4159367A (en) * | 1978-06-29 | 1979-06-26 | Yardney Electric Corporation | Hydrogen electrochemical cell and rechargeable metal-hydrogen battery |
| US4279970A (en) * | 1980-02-20 | 1981-07-21 | Electric Power Research Institute, Inc. | Electrochemical cell including ribbed electrode substrates |
| US4386987A (en) * | 1981-06-26 | 1983-06-07 | Diamond Shamrock Corporation | Electrolytic cell membrane/SPE formation by solution coating |
| US4411968A (en) * | 1981-09-30 | 1983-10-25 | United Technologies Corporation | Molten carbonate fuel cell integral matrix tape and bubble barrier |
| US4435267A (en) * | 1982-10-08 | 1984-03-06 | Exxon Research And Engineering Co. | Gas percolation barrier for gas fed electrode |
-
1984
- 1984-05-07 EP EP84105112A patent/EP0125595B1/en not_active Expired
- 1984-05-07 DE DE8484105112T patent/DE3465393D1/en not_active Expired
- 1984-05-07 US US06/607,786 patent/US4555324A/en not_active Expired - Lifetime
- 1984-05-08 CA CA000453757A patent/CA1218111A/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| DE3465393D1 (en) | 1987-09-17 |
| US4555324A (en) | 1985-11-26 |
| EP0125595A1 (en) | 1984-11-21 |
| EP0125595B1 (en) | 1987-08-12 |
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