WO2002069423A1 - Method for forming a membrane electrode diffusion assembly for use in an ion exchange membrane fuel cell - Google Patents

Method for forming a membrane electrode diffusion assembly for use in an ion exchange membrane fuel cell Download PDF

Info

Publication number
WO2002069423A1
WO2002069423A1 PCT/US2001/014071 US0114071W WO02069423A1 WO 2002069423 A1 WO2002069423 A1 WO 2002069423A1 US 0114071 W US0114071 W US 0114071W WO 02069423 A1 WO02069423 A1 WO 02069423A1
Authority
WO
WIPO (PCT)
Prior art keywords
diffusion layer
applying
electrolyte membrane
providing
ion conducting
Prior art date
Application number
PCT/US2001/014071
Other languages
French (fr)
Inventor
David R. Lott
P. David Devries
Original Assignee
Avista Laboratories, Inc.
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Priority claimed from US09/792,085 external-priority patent/US6383556B2/en
Application filed by Avista Laboratories, Inc. filed Critical Avista Laboratories, Inc.
Publication of WO2002069423A1 publication Critical patent/WO2002069423A1/en

Links

Classifications

    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/10—Fuel cells with solid electrolytes
    • H01M8/1004—Fuel cells with solid electrolytes characterised by membrane-electrode assemblies [MEA]
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00—Electrolytes
    • H01M2300/0017—Non-aqueous electrolytes
    • H01M2300/0065—Solid electrolytes
    • H01M2300/0082—Organic polymers
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30—Hydrogen technology
    • Y02E60/50—Fuel cells

Definitions

  • the present invention relates to a method for forming a membrane electrode diffusion assembly for use in an ion exchange membrane fuel cell.
  • a fuel cell generates electricity from a fuel source, such as hydrogen gas, and an oxidant such as oxygen or air.
  • a fuel source such as hydrogen gas
  • an oxidant such as oxygen or air.
  • the resulting chemical reaction does not result in a burning of the fuel, therefore the thermodynamic limits on the efficiency of such a chemical reaction are much greater than conventional power generation processes.
  • the fuel gas hydrogen
  • the hydrogen ions diffuse across the membrane to recombine with oxygen ions on the cathode.
  • the resulting byproduct of the reaction is water and the production of an electrical current.
  • a proton exchange membrane fuel cell power system which includes discrete and novel proton exchange membrane fuel cell modules which are self humidifying and which employ a membrane electrode diffusion assembly which provides increased reliability and other advantages not possible heretofore with respect to fuel cell designs which have been primarily directed to stack-type arrangements.
  • One aspect of the present invention is to provide a method for forming a membrane electrode diffusion assembly for use in an ion exchange membrane fuel cell which includes providing an ion conducting electrolyte membrane having opposite sides; and applying a first diffusion layer to one of the opposite sides of the ion conducting electrolyte membrane by the application of force sufficient to fabricate a resulting membrane electrode diffusion assembly which has an optimal operational temperature range when utilized in an ion exchange membrane fuel cell of less than about 95 degrees C.
  • Another aspect of the present invention relates to a method for forming a membrane electrode diffusion assembly for use in an ion exchange membrane fuel cell which includes providing an ion conducting electrolyte membrane having opposite anode and cathode sides; affixing an anode and cathode electrode on the respective anode and cathode sides; positioning a first diffusion layer on one of the anode and/or cathode sides of the ion conducting electrolyte membrane and in covering relation over the respective anode and/or cathode electrode; and applying a force of at least about 400 pounds to about 10,000 pounds per square inch to the first diffusion layer to affix the first diffusion layer on the ion conducting electrolyte membrane to form a resulting membrane electrode diffusion assembly.
  • another aspect of the present invention relates to a method of forming a membrane electrode diffusion assembly for use in an ion exchange membrane fuel cell, and which includes, first, providing an ion conducting electrolyte membrane having opposite anode and cathode sides; second, providing anode and cathode electrodes which are individually affixed on and located at least in partial covering relation relative to the respective anode and cathode sides of the electrolyte membrane; third, providing a first diffusion layer comprising carbon and a fluropolymer, and then heating the first diffusion layer to a temperature of about 100 degrees C to about 500 degrees C for a predetermined period of time in an oxygen-containing environment; fourth, affixing the previously heated first diffusion layer in at least partial covering relation relative to each of the anode and cathode electrodes by the application of pressure in the amount of about 400 pounds to about 10,000 pounds per square inch of surface area of the first diffusion layer; providing a permeable substrate having a predetermined thickness dimension and opposite sides; preparing a
  • Fig. 1 is a greatly enlarged, diagrammatic section of a membrane electrode diffusion assembly shown at one processing step in accordance with the present invention.
  • Fig. 2 is a greatly enlarged, diagrammatic section of a membrane electrode diffusion assembly shown at a processing step subsequent to that shown in Fig. 1.
  • Fig. 3 is a greatly enlarged, diagrammatic section of a membrane electrode diffusion assembly shown at a processing step subsequent to that shown in Fig. 2.
  • Fig. 4 is a greatly enlarged, diagrammatic section of a portion of a membrane electrode diffusion assembly at one processing step in accordance with the present invention.
  • Fig. 5 is a greatly enlarged, diagrammatic section of a portion of a membrane electrode diffusion assembly shown at a processing step subsequent to that shown in Fig. 4.
  • Fig. 6 is a greatly enlarged, diagrammatic section of a membrane electrode diffusion assembly at a processing step subsequent to that shown in Fig. 5.
  • ion conducting electrolyte membrane having opposite sides 11 and 12 is shown.
  • the term "ion conducting electrolyte membrane” is defined as a proton or anion conducting membrane either alone, or in combination with other materials.
  • side 1 1 is the anode side
  • side 12 is designated as the cathode side.
  • a suitable proton-conducting membrane may be purchased from the W.L. Gore Company under the trade designation Primea 6000 series. Of course any membrane which allows for the movement of protons or anions across the membrane interface may be potentially suitable for use.
  • the ion conducting electrolyte membrane is shown at a second step in the method wherein individual anode and cathode electrodes designated by the numerals 20 and 30 are affixed on the opposite anode and cathode sides 1 1 and 12, respectively, thereby placing them in ionic contact with the underlying ion conducting electrolyte membrane 10.
  • the anode and cathode electrodes are located at least in partial covering relation relative to the respective anode and cathode sides 11 and 12 of the electrolyte membrane.
  • the anode and cathode electrodes are provided before any of the following steps are conducted. Referring now to Fig.
  • the method further includes providing a first diffusion layer 40 which comprises carbon and a fluropolymer.
  • This first diffusion layer is first heated to a temperature of about 100 degrees C to about 500 degrees C in an oxygen-containing environment such as air for a predetermined period of time which lies in a range of about 1 second to about 2 minutes.
  • the first diffusion layer is positioned at least in partial covering relation relative to each of the anode and cathode electrodes 20 and 30 and is affixed thereto by the application of pressure in the amount of about 400 pounds to about 10,000 pounds per square inch of surface area of the first diffusion layer.
  • the carbon portion of the first diffusion layer 40 is selected from the group consisting essentially of carbon cloth, carbon paper or carbon sponge or a suitable equivalent.
  • the fluropolymer is selected from the group consisting essentially of perfluorinated hydrocarbons or suitable equivalents. The resulting combination of these two materials results in a first diffusion layer 40 which is rendered substantially hydrophobic.
  • first diffusion layer 40 may be attached first to the anode, or alternatively to the cathode electrode, or further may be attached simultaneously to both the anode and cathode electrodes by the application of a force of about 400 pounds to about 10,000 pounds per square inch.
  • a porous substrate 50 is provided and which is selected from the group consisting essentially of carbon cloth, carbon paper or carbon sponge or a suitable equivalent.
  • the porous substrate 50 has a thickness of about 0.2 mm to about 2.0 mm.
  • a slurry is later prepared and which comprises at least about 20% to about 90% by weight of a particulate carbon and a hydrophobic binding resin dispersed in a water solution which may contain a small amount of a surfactant such as an alcohol.
  • the slurry 60 is applied to coat one of the sides of the permeable substrate 50.
  • an air drying step is conducted to evaporate the water and any surfactant, and thereby deposit the particulate carbon and hydrophobic resin on the coated side.
  • additional coats of the slurry 60 are applied, each separated by the aforementioned air drying step to form a second diffusion layer 70 (Fig. 5) having a resulting hydrophobic gradient.
  • the second diffusion layer 70 is positioned in juxtaposed covering relation relative to the first diffusion layer 40 and affixed thereto to form a resulting membrane electrode diffusion assembly 100.
  • the hydrophobic binding resin selected for use in the second diffusion layer can be selected from the group including perfluorinated hydrocarbons.
  • the method of the present invention includes providing an ion conducting electrolyte membrane 10 having opposite anode and cathode sides 1 1 and 12, respectively.
  • the method further includes, third, providing a first diffusion layer 40 comprising carbon and a fluropolymer and then heating the first diffusion layer to a temperature of about 100 degrees C to about 500 degrees C for a predetermined period of time in an oxygen-containing environment such as air. Following the heating of the first diffusion layer, affixing the previously heated first diffusion layer in at least partial covering relation relative to the anode and cathode electrodes 20 and 30 by the application of pressure in the amount of about 400 pounds to about 10,000 pounds per square inch of surface are of the first diffusion layer. As seen in Fig. 4, the method of the present invention further includes, providing a permeable substrate 50 having a predetermined thickness dimension and opposite sides.
  • the method further includes preparing a slurry comprising at least 20% to about 90% by weight of a particular carbon and a hydrophobic binding resin dispersed in a water solution which may include a surfactant such as alcohol, and applying the slurry to coat one of the sides of the permeable substrate 50.
  • the method further includes a step of air drying the coated side of the porous substrate, and after the step of air drying the coated side, applying additional coats of the slurry, each separated by the aforementioned air drying step, to form a second diffusion layer 70 (Fig. 5) having a resulting hydrophobic gradient.
  • the method further includes positioning the second diffusion layer in juxtaposed covering relation relative to the first diffusion layer 40. This forms a resulting membrane electrode diffusion assembly 100 for use in an ion exchange membrane fuel cell.

Abstract

A method for forming a membrane electrode diffusion assembly for use in an ion exchange membrane fuel cell is described and which includes, providing an ion conducting electrolyte membrane (10) having opposite sides (11, 12), and applying a first diffusion layer (40) to one of the opposite sides of the membrane by application of force sufficient to fabricate a resulting membrane electrode diffusion assembly which has an optimal temperature range when used in an ion exchange membrane fuel cell of less than about 95 degrees C.

Description

DESCRIPTION
METHOD FOR FORMING A MEMBRANE ELECTRODE DIFFUSION
ASSEMBLY FOR USE IN AN ION EXCHANGE MEMBRANE FUEL CELL
Technical Field
This application is a continuation in part of Application Serial No. 09/577,407 which was filled on May 17, 2000. The present invention relates to a method for forming a membrane electrode diffusion assembly for use in an ion exchange membrane fuel cell.
Background Art
The operation of fuel cells are well known. In this regard, a fuel cell generates electricity from a fuel source, such as hydrogen gas, and an oxidant such as oxygen or air. The resulting chemical reaction does not result in a burning of the fuel, therefore the thermodynamic limits on the efficiency of such a chemical reaction are much greater than conventional power generation processes. In a proton exchange membrane fuel cell the fuel gas (hydrogen) is ionized on one electrode, and the hydrogen ions diffuse across the membrane to recombine with oxygen ions on the cathode. The resulting byproduct of the reaction is water and the production of an electrical current.
In U.S. Patent No. 6,030,718, the teachings of which are incorporated by reference herein, a proton exchange membrane fuel cell power system is disclosed and which includes discrete and novel proton exchange membrane fuel cell modules which are self humidifying and which employ a membrane electrode diffusion assembly which provides increased reliability and other advantages not possible heretofore with respect to fuel cell designs which have been primarily directed to stack-type arrangements. While this prior art patent discloses a method of producing a suitable membrane electrode diffusion assembly which operates with a great deal of success, the inventors have endeavored to improve upon this inventive concept by focusing further investigation on a method of manufacturing a membrane electrode diffusion assembly which increases the performance, and versatility of same and which further may be utilized in a modular design such as disclosed in this previous patent, or which may be also utilized in more traditional stack-type arrangements. Accordingly, a method for forming a membrane electrode diffusion assembly for use in an ion exchange membrane fuel cell which achieves the benefits to be derived from the aforementioned teaching is the subject matter of the present invention.
Summary of the Invention
One aspect of the present invention is to provide a method for forming a membrane electrode diffusion assembly for use in an ion exchange membrane fuel cell which includes providing an ion conducting electrolyte membrane having opposite sides; and applying a first diffusion layer to one of the opposite sides of the ion conducting electrolyte membrane by the application of force sufficient to fabricate a resulting membrane electrode diffusion assembly which has an optimal operational temperature range when utilized in an ion exchange membrane fuel cell of less than about 95 degrees C. Another aspect of the present invention relates to a method for forming a membrane electrode diffusion assembly for use in an ion exchange membrane fuel cell which includes providing an ion conducting electrolyte membrane having opposite anode and cathode sides; affixing an anode and cathode electrode on the respective anode and cathode sides; positioning a first diffusion layer on one of the anode and/or cathode sides of the ion conducting electrolyte membrane and in covering relation over the respective anode and/or cathode electrode; and applying a force of at least about 400 pounds to about 10,000 pounds per square inch to the first diffusion layer to affix the first diffusion layer on the ion conducting electrolyte membrane to form a resulting membrane electrode diffusion assembly.
Yet further, another aspect of the present invention relates to a method of forming a membrane electrode diffusion assembly for use in an ion exchange membrane fuel cell, and which includes, first, providing an ion conducting electrolyte membrane having opposite anode and cathode sides; second, providing anode and cathode electrodes which are individually affixed on and located at least in partial covering relation relative to the respective anode and cathode sides of the electrolyte membrane; third, providing a first diffusion layer comprising carbon and a fluropolymer, and then heating the first diffusion layer to a temperature of about 100 degrees C to about 500 degrees C for a predetermined period of time in an oxygen-containing environment; fourth, affixing the previously heated first diffusion layer in at least partial covering relation relative to each of the anode and cathode electrodes by the application of pressure in the amount of about 400 pounds to about 10,000 pounds per square inch of surface area of the first diffusion layer; providing a permeable substrate having a predetermined thickness dimension and opposite sides; preparing a slurry comprising at least about 20% to about 90% by weight of a particulate carbon and a hydrophobic binding resin dispersed in a water solution which may include surfactant, and applying the slurry to coat one of the sides of the permeable substrate; air drying the coated side of the porous substrate, and after the step of air drying the coated side, applying additional coats of the slurry, each separated by the aforementioned air drying step, to form a second diffusion layer having a resulting hydrophobic gradient; and positioning the second diffusion layer in juxtaposed covering relation relative to the first diffusion layer.
These and other aspects of the present invention will be discussed in further detail hereinafter.
Detailed Description of the Drawings Preferred embodiments of the invention are described below with reference to the following accompanying drawings.
Fig. 1 is a greatly enlarged, diagrammatic section of a membrane electrode diffusion assembly shown at one processing step in accordance with the present invention. Fig. 2 is a greatly enlarged, diagrammatic section of a membrane electrode diffusion assembly shown at a processing step subsequent to that shown in Fig. 1.
Fig. 3 is a greatly enlarged, diagrammatic section of a membrane electrode diffusion assembly shown at a processing step subsequent to that shown in Fig. 2.
Fig. 4 is a greatly enlarged, diagrammatic section of a portion of a membrane electrode diffusion assembly at one processing step in accordance with the present invention.
Fig. 5 is a greatly enlarged, diagrammatic section of a portion of a membrane electrode diffusion assembly shown at a processing step subsequent to that shown in Fig. 4. Fig. 6 is a greatly enlarged, diagrammatic section of a membrane electrode diffusion assembly at a processing step subsequent to that shown in Fig. 5.
Best Modes for Carrying Out the Invention and Disclosure of Invention This disclosure of the invention is submitted in furtherance of the constitutional purposes of the U.S. Patent Laws "to promote the progress of science and useful arts" (Article 1, Section 8).
Referring now to Fig. 1, an ion conducting electrolyte membrane having opposite sides 11 and 12 is shown. In the context of this document the term "ion conducting electrolyte membrane" is defined as a proton or anion conducting membrane either alone, or in combination with other materials. As seen in Fig. 1 side 1 1 is the anode side, and side 12 is designated as the cathode side. As discussed in U.S. Patent No. 6,030,718 a suitable proton-conducting membrane may be purchased from the W.L. Gore Company under the trade designation Primea 6000 series. Of course any membrane which allows for the movement of protons or anions across the membrane interface may be potentially suitable for use.
Referring now to Fig. 2, the ion conducting electrolyte membrane is shown at a second step in the method wherein individual anode and cathode electrodes designated by the numerals 20 and 30 are affixed on the opposite anode and cathode sides 1 1 and 12, respectively, thereby placing them in ionic contact with the underlying ion conducting electrolyte membrane 10. As seen, the anode and cathode electrodes are located at least in partial covering relation relative to the respective anode and cathode sides 11 and 12 of the electrolyte membrane. The anode and cathode electrodes are provided before any of the following steps are conducted. Referring now to Fig. 3, following the step of providing the anode and cathode electrodes 20 and 30 which are individually affixed on, and located at least in partial covering relation relative to, the respective anode and cathode sides of the electrolyte membrane, the method further includes providing a first diffusion layer 40 which comprises carbon and a fluropolymer. This first diffusion layer is first heated to a temperature of about 100 degrees C to about 500 degrees C in an oxygen-containing environment such as air for a predetermined period of time which lies in a range of about 1 second to about 2 minutes. Subsequent to the heating step noted above, the first diffusion layer is positioned at least in partial covering relation relative to each of the anode and cathode electrodes 20 and 30 and is affixed thereto by the application of pressure in the amount of about 400 pounds to about 10,000 pounds per square inch of surface area of the first diffusion layer. The carbon portion of the first diffusion layer 40 is selected from the group consisting essentially of carbon cloth, carbon paper or carbon sponge or a suitable equivalent. Yet further, the fluropolymer is selected from the group consisting essentially of perfluorinated hydrocarbons or suitable equivalents. The resulting combination of these two materials results in a first diffusion layer 40 which is rendered substantially hydrophobic. It should be recognized that in the step of affixing the first diffusion layer 40 to the underlying anode and cathode electrodes 20 and 30 that such first diffusion layer 40 may be attached first to the anode, or alternatively to the cathode electrode, or further may be attached simultaneously to both the anode and cathode electrodes by the application of a force of about 400 pounds to about 10,000 pounds per square inch.
Referring now to Fig. 4, a porous substrate 50 is provided and which is selected from the group consisting essentially of carbon cloth, carbon paper or carbon sponge or a suitable equivalent. The porous substrate 50 has a thickness of about 0.2 mm to about 2.0 mm. As seen in Fig. 4, and then subsequently in Fig. 5, a slurry is later prepared and which comprises at least about 20% to about 90% by weight of a particulate carbon and a hydrophobic binding resin dispersed in a water solution which may contain a small amount of a surfactant such as an alcohol. As seen in Fig. 4, the slurry 60 is applied to coat one of the sides of the permeable substrate 50. Thereafter, an air drying step is conducted to evaporate the water and any surfactant, and thereby deposit the particulate carbon and hydrophobic resin on the coated side. Thereafter, as seen in Fig. 5, additional coats of the slurry 60 are applied, each separated by the aforementioned air drying step to form a second diffusion layer 70 (Fig. 5) having a resulting hydrophobic gradient.
Referring now to Fig. 6, it will be seen that the second diffusion layer 70 is positioned in juxtaposed covering relation relative to the first diffusion layer 40 and affixed thereto to form a resulting membrane electrode diffusion assembly 100. It should be understood that the hydrophobic binding resin selected for use in the second diffusion layer can be selected from the group including perfluorinated hydrocarbons.
The operation of the described embodiment of the present invention is believed to be readily apparent and is briefly summarized at this point.
Referring now to Fig. 1, a method for forming a resulting membrane electrode diffusion assembly 100 for use in an ion exchange membrane fuel cell is illustrated, and in a first step, the method of the present invention includes providing an ion conducting electrolyte membrane 10 having opposite anode and cathode sides 1 1 and 12, respectively. Second, after providing the ion conducting electrolyte membrane, providing anode and cathode electrodes 20 and 30 respectively which are individually affixed on and located at least in partial covering relation relative to the respective anode and cathode sides of the electrolyte membrane 10. The method further includes, third, providing a first diffusion layer 40 comprising carbon and a fluropolymer and then heating the first diffusion layer to a temperature of about 100 degrees C to about 500 degrees C for a predetermined period of time in an oxygen-containing environment such as air. Following the heating of the first diffusion layer, affixing the previously heated first diffusion layer in at least partial covering relation relative to the anode and cathode electrodes 20 and 30 by the application of pressure in the amount of about 400 pounds to about 10,000 pounds per square inch of surface are of the first diffusion layer. As seen in Fig. 4, the method of the present invention further includes, providing a permeable substrate 50 having a predetermined thickness dimension and opposite sides. Following providing the permeable substrate, the method further includes preparing a slurry comprising at least 20% to about 90% by weight of a particular carbon and a hydrophobic binding resin dispersed in a water solution which may include a surfactant such as alcohol, and applying the slurry to coat one of the sides of the permeable substrate 50. Subsequently, the method further includes a step of air drying the coated side of the porous substrate, and after the step of air drying the coated side, applying additional coats of the slurry, each separated by the aforementioned air drying step, to form a second diffusion layer 70 (Fig. 5) having a resulting hydrophobic gradient. As seen in Fig. 6, and following the formation of the second diffusion layer 70, the method further includes positioning the second diffusion layer in juxtaposed covering relation relative to the first diffusion layer 40. This forms a resulting membrane electrode diffusion assembly 100 for use in an ion exchange membrane fuel cell.
In compliance with the statute, the invention has been described in language more or less specific as to structural and methodical features. It is to be understood, however, that the invention is not limited to the specific features shown and described, since the means herein disclosed comprise preferred forms of putting the invention into effect. The invention is, therefore, claimed in any of its forms or modifications within the proper scope of the appended claims appropriately interpreted in accordance with the doctrine of equivalents.

Claims

1. A method for forming a membrane electrode diffusion assembly for use in an ion exchange membrane fuel cell, comprising: providing an ion conducting electrolyte membrane having opposite sides; and applying a first diffusion layer to one of the opposite sides of the ion conducting electrolyte membrane by the application of force sufficient to fabricate a resulting membrane electrode diffusion assembly which has an optimal operational temperature range when utilized in an ion exchange membrane fuel cell of less than about 95 degrees C.
2. A method as claimed in claim 1, and further comprising: before applying the first diffusion layer, and after providing the ion conducting electrolyte membrane, providing anode and cathode electrodes which are individually located in covering relation on the opposite sides of the ion conducting electrolyte membrane, and wherein the first diffusion layer is located in covering relation relative to the anode and cathode electrodes.
3. A method as claimed in claim 1, wherein the first diffusion layer is applied with a force of at least about 400 pounds to about 10,000 pounds per square inch.
4. A method as claimed in claim 1, and further providing anode and cathode electrodes individually disposed on the opposite sides of the ion conducting electrolyte membrane, and wherein the first diffusion layer is applied to the side of the ion conducting electrolyte membrane bearing the anode electrode with a force of at least about 400 pounds to about 10,000 pounds per square inch.
5. A method as claimed in claim 1, and further providing anode and cathode electrodes individually disposed on the opposite sides of the ion conducting electrolyte membrane, and wherein the first diffusion layer is applied to the side of the ion conducting electrolyte membrane bearing the cathode electrode with a force of at least about 400 pounds to about 10,000 pounds per square inch.
6. A method as claimed in claim 1, and further providing anode and cathode electrodes individually disposed on the opposite sides of the ion conducting electrolyte membrane, and wherein the first diffusion layer is applied concurrently to both sides of the ion conducting electrolyte membrane with a force of at least about 400 pounds to about 10,000 pounds per square inch.
7. A method as claimed in claim 1, and further comprising: providing anode and cathode electrodes individually disposed on the opposite sides of the ion conducting electrolyte membrane, and wherein the first diffusion layer comprises carbon and a fluropolymer which is applied to both sides of the ion conducting electrolyte membrane, and in covering relation relative the respective anode and cathode electrodes with a force of at least about 400 to about 10,000 pounds per square inch.
8 A method as claimed in claim 6, and further comprising: after the step of providing the ion conducting electrolyte membrane and applying the first diffusion layer thereto, providing a permeable substrate; and applying a porous layer to the porous substrate to form a second diffusion layer.
9. A method as claimed in claim 6, and further comprising: after the step of applying the first diffusion layer, providing a permeable substrate; and applying a porous layer to the permeable substrate and which comprises at least about 20% to about 90% by weight of particulate carbon and a hydrophobic binding resin which forms a second diffusion layer.
10. A method as claimed in claim 9, wherein the step of applying the porous layer to the permeable substrate to form the second diffusion layer further comprises: applying the porous layer to the permeable substrate in the form of a slurry which is applied in successive coats to form a hydrophobic gradient.
11. A method as claimed in claim 1, and further comprising: before the step of applying the first diffusion layer, providing a permeable substrate; and applying a porous layer thereto in the form of a slurry which comprises carbon and a hydrophobic binding resin to form a second diffusion layer which has a hydrophobic gradient; and applying the first diffusion layer to the ion conducting electrolyte membrane with a force of at least about 400 pounds to about 10,000 pounds per square inch, and wherein following the step of applying force to the first diffusion layer, positioning the second diffusion layer in covering relation relative to the first diffusion layer.
12. A method as claimed in claim 1, and further comprising: before the step of applying the first diffusion layer, heating the first diffusion layer to a predetermined temperature, and wherein the first diffusion layer is applied to the electrolyte membrane with a force of at least about 400 pounds per square inch to about 10,000 pounds per square inch.
13. A method as claimed in claim 1, and wherein the first diffusion layer comprises carbon and a fluropolymer, and wherein before the step of applying the first diffusion layer, heating the first diffusion layer to a temperature of about 100 degrees C to about 500 degrees C in the presence of air; and wherein the first diffusion layer is applied to the ion conducting electrolyte membrane with a force of at least about 400 pounds to about 10,000 pounds per square inch.
14. A method as claimed in claim 1, and further comprising: before the step of applying the first diffusion layer, providing anode and cathode electrodes individually disposed on the opposite sides of the ion conducting electrolyte membrane, and wherein the first diffusion layer comprises carbon and a fluropolymer; heating the first diffusion layer to a temperature of about 100 degrees C to about 500 degrees C, and wherein after the step of heating the first diffusion layer, positioning the first diffusion layer in covering relation relative to the respective anode and cathode electrodes; and applying the first diffusion layer to the ion conducting electrolyte membrane by the application of a force of about 400 pounds to about 10,000 pounds per square inch to the ion conducting electrolyte membrane and the first diffusion layer.
15. A method as claimed in claim 14, and further comprising: after the step of applying the first diffusion layer, providing a permeable substrate; and applying a porous layer to the permeable substrate and which comprises at least about 20% to about 90% by weight of particulate carbon and a hydrophobic binding resin which forms a resulting second diffusion layer; and positioning the second diffusion layer in covering relation relative to the first diffusion layer.
16. A method as claimed in claim 15, wherein the step of applying the porous layer to the permeable substrate further comprises: applying the porous layer in a slurry onto the permeable substrate in successive coats to form a hydrophobic gradient.
17. A method as claimed in claim 16, wherein each successive coat of the porous layer forming the second diffusion layer is air dried prior to the application of a subsequent coat.
18. A method for forming a membrane electrode diffusion assembly for use in an ion exchange membrane fuel, comprising: providing an ion conducting electrolyte membrane having opposite anode and cathode sides; affixing an anode and cathode electrode on the respective anode and cathode sides; positioning a first diffusion layer on one of the anode and/or cathode sides of the ion conducting electrolyte membrane and in covering relation over the respective anode and/or cathode electrode; and applying a force of at least about 400 pounds to about 10,000 pounds per square inch to the first diffusion layer to affix the first diffusion layer on the ion conducting electrolyte membrane to form a membrane electrode diffusion assembly.
19. A method as claimed in claim 18, and wherein the membrane electrode diffusion assembly is incorporated into an ion exchange membrane fuel cell which has a cathode air flow, and wherein the ion exchange membrane fuel cell has a power output, and wherein the method further comprises: exposing the cathode side of the membrane electrode diffusion assembly to the cathode air flow, and wherein the power output of the ion exchange membrane fuel cell is not substantially degraded upon exposure of the cathode side of the membrane electrode diffusion assembly to cathode air flow temperatures of less than about 95 degrees C.
20. A method as claimed in claim 19, and wherein the first diffusion layer comprises carbon and a fluropolymer, and wherein before the step of affixing the first diffusion layer the method further comprises: heating the first diffusion layer to a temperature of about 100 degrees C to about 500 degrees C in the presence of air.
21. A method as claimed in claim 20 and further comprising: after the step of providing the ion conducting electrolyte membrane and affixing the first diffusion layer thereto, providing a permeable substrate; and applying a porous layer to the permeable substrate to form a second diffusion layer.
22. A method as claimed in claim 20, and further comprising: after the step of applying the first diffusion layer, providing a permeable substrate; and applying a porous layer to the permeable substrate and which comprises at least about 20% to about 90 % by weight of particulate carbon and a hydrophobic binding resin, and which forms a second diffusion layer.
23. A method as claimed in claim 22, wherein the step of applying the porous layer to the permeable substrate further comprises: applying the porous layer in the form of a slurry to the permeable substrate in successive coats to form a resulting hydrophobic gradient in the second diffusion layer.
24. A method for forming a membrane electrode diffusion assembly for use in an ion exchange membrane fuel cell, comprising: first, providing an ion conducting electrolyte membrane having opposite anode and cathode sides; second, providing anode and cathode electrodes which are individually affixed on, and located at least in partial covering relation relative to the respective anode and cathode sides of the electrolyte membrane; third, providing a first diffusion layer comprising carbon and a fluropolymer, and then heating the first diffusion layer to a temperature of about 100 degrees C to about 500 degrees C for a predetermined period of time in the presence of air; fourth, affixing the previously heated first diffusion layer in at least partial covering relation relative to each of the anode and cathode electrodes by the application of pressure in the amount of about 400 pounds to about 10,000 pounds per square inch of surface area of the first diffusion layer; providing a permeable substrate having a predetermined thickness dimension and opposite sides; preparing a slurry comprising at least about 20% to about 90% by weight of a particulate carbon and a hydrophobic binding resin dispersed in a water solution, and applying the slurry to coat one of the sides of the permeable substrate; air drying the coated side of the porous substrate, and after the step of air drying the coated side, applying additional coats of the slurry, each separated by the aforementioned air drying step, to form a second diffusion layer having a resulting hydrophobic gradient; and positioning the second diffusion layer in juxtaposed, covering relation relative to the first diffusion layer.
PCT/US2001/014071 2001-02-23 2001-05-01 Method for forming a membrane electrode diffusion assembly for use in an ion exchange membrane fuel cell WO2002069423A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US09/792,085 US6383556B2 (en) 2000-05-17 2001-02-23 Method for forming a membrane electrode diffusion assembly for use in an ion exchange membrane fuel cell
US09/792,085 2001-02-23

Publications (1)

Publication Number Publication Date
WO2002069423A1 true WO2002069423A1 (en) 2002-09-06

Family

ID=25155744

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US2001/014071 WO2002069423A1 (en) 2001-02-23 2001-05-01 Method for forming a membrane electrode diffusion assembly for use in an ion exchange membrane fuel cell

Country Status (1)

Country Link
WO (1) WO2002069423A1 (en)

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5346780A (en) * 1991-11-25 1994-09-13 Kabushiki Kaisha Toshiba Fuel cell and method for producing an electrode used therefor
US5399184A (en) * 1992-05-01 1995-03-21 Chlorine Engineers Corp., Ltd. Method for fabricating gas diffusion electrode assembly for fuel cells
US5607785A (en) * 1995-10-11 1997-03-04 Tanaka Kikinzoku Kogyo K.K. Polymer electrolyte electrochemical cell and process of preparing same
EP0935304A1 (en) * 1998-02-06 1999-08-11 Matsushita Electric Industrial Co., Ltd. Polymer electrolyte fuel cell and preparation method for polymer electrolyte fuel cell
EP0955687A2 (en) * 1998-05-04 1999-11-10 Samsung Electronics Co., Ltd. Method for producing a slurry for forming a catalyst layer for a proton exchange membrane fuel cell
US6030718A (en) * 1997-11-20 2000-02-29 Avista Corporation Proton exchange membrane fuel cell power system
US6106965A (en) * 1996-03-29 2000-08-22 Mazda Motor Corporation Polymer electrolyte fuel cell

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5346780A (en) * 1991-11-25 1994-09-13 Kabushiki Kaisha Toshiba Fuel cell and method for producing an electrode used therefor
US5399184A (en) * 1992-05-01 1995-03-21 Chlorine Engineers Corp., Ltd. Method for fabricating gas diffusion electrode assembly for fuel cells
US5607785A (en) * 1995-10-11 1997-03-04 Tanaka Kikinzoku Kogyo K.K. Polymer electrolyte electrochemical cell and process of preparing same
US6106965A (en) * 1996-03-29 2000-08-22 Mazda Motor Corporation Polymer electrolyte fuel cell
US6030718A (en) * 1997-11-20 2000-02-29 Avista Corporation Proton exchange membrane fuel cell power system
EP0935304A1 (en) * 1998-02-06 1999-08-11 Matsushita Electric Industrial Co., Ltd. Polymer electrolyte fuel cell and preparation method for polymer electrolyte fuel cell
EP0955687A2 (en) * 1998-05-04 1999-11-10 Samsung Electronics Co., Ltd. Method for producing a slurry for forming a catalyst layer for a proton exchange membrane fuel cell

Similar Documents

Publication Publication Date Title
US6383556B2 (en) Method for forming a membrane electrode diffusion assembly for use in an ion exchange membrane fuel cell
JP4522502B2 (en) Gas diffusion electrodes for polymer membrane fuel cells
US6106965A (en) Polymer electrolyte fuel cell
US5869202A (en) Hydrophillic graphite fuel cell electrode for use with an ionomer membrane fuel cell
US20020058172A1 (en) Method of producing a membrane electrode assembly, and membrane electrode assembly produced using this method, as well as associated fuel cell battery
JP4738350B2 (en) Method of manufacturing a durable membrane electrode assembly in which the catalyst-coated diffusion medium is not bonded to the membrane
JP2012074353A (en) Partially hydrophilic gas diffusion layer and fuel cell stack including the same
JP2003109606A (en) High molecular electrolyte fuel cell and method of manufacturing the same
JP4766014B2 (en) Manufacturing method of membrane electrode assembly
JP2007524973A (en) Membrane electrode assembly prepared by spraying catalyst directly onto membrane
JP3356465B2 (en) Method for manufacturing electrode for solid polymer electrolyte fuel cell
JP2000299119A (en) Manufacture of catalyst layer
JP2000003718A (en) Method for activating high molecular electrolyte fuel cell
JP2011520237A (en) Method for activating membrane electrode assembly, membrane electrode assembly and polymer electrolyte fuel cell using the same
WO2002069423A1 (en) Method for forming a membrane electrode diffusion assembly for use in an ion exchange membrane fuel cell
JP3965666B2 (en) Gas diffusion electrode and manufacturing method thereof
JPH08138715A (en) Solid polymer fuel cell and manufacture thereof
JP2004185900A (en) Electrode for fuel cell, film/catalyst layer junction, fuel cell, and manufacturing method of them
JPH05190184A (en) Electrode-electrolyte joint body, manufacture thereof, and fuel cell using thereof
JPH06150944A (en) Fuel cell electrode
JP2023127406A (en) Manufacturing method of membrane/electrode assembly
KR100343117B1 (en) Fabrication method of the self-humidified polymer membrane and self-humidified polymer membrane/electrode assembly for polymer electrolyte membrane cell
Umap et al. Performance of Catalyst Coated Membrane (CCM) at different operating conditions in Proton Exchange Membrane (PEM) fuel cell
KR100508890B1 (en) Monolithic collector-electrode for direct methanol fuel cell using carbon cloth with built-in metal lines and method for manufacturing the same
KR100393283B1 (en) Polymer electrolyte membrane/electrode assembly with metal wire end in it, and its manufacturing method for polymer electrolyte membrane fuel cell

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EE ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NO NZ PL PT RO RU SD SE SG SI SK SL TJ TM TR TT TZ UA UG US UZ VN YU ZA ZW

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): GH GM KE LS MW MZ SD SL SZ TZ UG ZW AM AZ BY KG KZ MD RU TJ TM AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE TR BF BJ CF CG CI CM GA GN GW ML MR NE SN TD TG

121 Ep: the epo has been informed by wipo that ep was designated in this application
REG Reference to national code

Ref country code: DE

Ref legal event code: 8642

122 Ep: pct application non-entry in european phase
NENP Non-entry into the national phase

Ref country code: JP