WO1999004445A1 - Process for producing polybenzimidazole pastes and gels for use in fuel cells - Google Patents

Process for producing polybenzimidazole pastes and gels for use in fuel cells Download PDF

Info

Publication number
WO1999004445A1
WO1999004445A1 PCT/US1998/010464 US9810464W WO9904445A1 WO 1999004445 A1 WO1999004445 A1 WO 1999004445A1 US 9810464 W US9810464 W US 9810464W WO 9904445 A1 WO9904445 A1 WO 9904445A1
Authority
WO
WIPO (PCT)
Prior art keywords
paste
gel
weight
acid
pbi
Prior art date
Application number
PCT/US1998/010464
Other languages
French (fr)
Inventor
Frank J. Onorato
Michael J. Sansone
Stuart M. French
Faruq Marikar
Original Assignee
Aventis Research And Technologies Gmbh & Kg
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
Application filed by Aventis Research And Technologies Gmbh & Kg filed Critical Aventis Research And Technologies Gmbh & Kg
Priority to EP98924836A priority Critical patent/EP0996990B1/en
Priority to KR20007000460A priority patent/KR100511152B1/en
Priority to DK98924836T priority patent/DK0996990T3/en
Priority to CA002306481A priority patent/CA2306481C/en
Priority to BR9811508-1A priority patent/BR9811508A/en
Priority to AU76914/98A priority patent/AU7691498A/en
Priority to JP2000503566A priority patent/JP4754687B2/en
Priority to AT98924836T priority patent/ATE251805T1/en
Priority to DE69818826T priority patent/DE69818826T2/en
Publication of WO1999004445A1 publication Critical patent/WO1999004445A1/en

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/10Fuel cells with solid electrolytes
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/02Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/02Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques
    • C08J3/09Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques in organic liquids
    • C08J3/091Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques in organic liquids characterised by the chemical constitution of the organic liquid
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/02Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques
    • C08J3/09Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques in organic liquids
    • C08J3/091Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques in organic liquids characterised by the chemical constitution of the organic liquid
    • C08J3/095Oxygen containing compounds
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/02Details
    • H01M8/0289Means for holding the electrolyte
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/10Fuel cells with solid electrolytes
    • H01M8/1016Fuel cells with solid electrolytes characterised by the electrolyte material
    • H01M8/1018Polymeric electrolyte materials
    • H01M8/102Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer
    • H01M8/1027Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer having carbon, oxygen and other atoms, e.g. sulfonated polyethersulfones [S-PES]
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/10Fuel cells with solid electrolytes
    • H01M8/1016Fuel cells with solid electrolytes characterised by the electrolyte material
    • H01M8/1018Polymeric electrolyte materials
    • H01M8/102Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer
    • H01M8/103Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer having nitrogen, e.g. sulfonated polybenzimidazoles [S-PBI], polybenzimidazoles with phosphoric acid, sulfonated polyamides [S-PA] or sulfonated polyphosphazenes [S-PPh]
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/10Fuel cells with solid electrolytes
    • H01M8/1016Fuel cells with solid electrolytes characterised by the electrolyte material
    • H01M8/1018Polymeric electrolyte materials
    • H01M8/1041Polymer electrolyte composites, mixtures or blends
    • H01M8/1046Mixtures of at least one polymer and at least one additive
    • H01M8/1048Ion-conducting additives, e.g. ion-conducting particles, heteropolyacids, metal phosphate or polybenzimidazole with phosphoric acid
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/10Fuel cells with solid electrolytes
    • H01M8/1016Fuel cells with solid electrolytes characterised by the electrolyte material
    • H01M8/1018Polymeric electrolyte materials
    • H01M8/1069Polymeric electrolyte materials characterised by the manufacturing processes
    • H01M8/1081Polymeric electrolyte materials characterised by the manufacturing processes starting from solutions, dispersions or slurries exclusively of polymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2379/00Characterised by the use of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen with or without oxygen, or carbon only, not provided for in groups C08J2361/00 - C08J2377/00
    • C08J2379/04Polycondensates having nitrogen-containing heterocyclic rings in the main chain; Polyhydrazides; Polyamide acids or similar polyimide precursors
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00Electrolytes
    • H01M2300/0085Immobilising or gelification of electrolyte
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

Definitions

  • This invention relates to the manufacture of a paste or gel for use as a polymer electrolyte in fuel cell applications.
  • Fuel cells can be configured in numerous ways with a variety of electrolytes, fuels and operating temperatures.
  • fuels such as hydrogen or methanol can be provided directly to the fuel cell electrode.
  • fuels such as methane or methanol, can be converted to a hydrogen rich gas mixture external to the cell itself and subsequently provided to the fuel cell.
  • Air is the source of oxygen in most fuel cells, although in some applications, the oxygen is obtained by hydrogen peroxide decomposition or from a cryogenic storage system.
  • PBI polybenzimidazole
  • the present invention provides a method of preparing a polymeric, preferably PBI, paste or gel for use as an electrolyte in fuel cells.
  • the method comprises soaking finely divided
  • PBI polymer in a suitable amount of an acid solution which permits the polymer to dissolve and form a matrix having a gel-like or paste-like consistency at room temperature.
  • the present invention provides a PBI paste or gel, which contains between about 70 to about 99.9% by weight of imbibed acid, which paste or gel is useful in fuel cells.
  • PBI paste or gel which contains between about 70 to about 99.9% by weight of imbibed acid, which paste or gel is useful in fuel cells.
  • the invention provides a polymeric fabric coated with a PBI paste or gel according to the invention.
  • the invention provides a fuel cell comprising a PBI paste or gel, or coated fabric, according to this invention.
  • the present invention provides a polymeric film coated with a PBI paste or gel of the invention.
  • the present invention provides a polymeric film coated with a PBI paste or gel of the invention with a second polymeric film forming a sandwich structure.
  • the present invention provides a method for preparing an electrode for use in fuel cells by steps which include coating the electrode with a paste or gel of the invention.
  • the present invention provides an improvement over the art in methods of preparing a polymeric paste or gel which contains acid and is useful as an electrolyte in fuel cells, particularly chlorine-resistant fuel cells, and in the preparation of adhesives. Also provided are the pastes or gels prepared by the method of the invention, as well as fabric and film coated thereby, and fuel cells containing the pastes or gels of the invention.
  • a polymeric paste or gel is prepared by mixing or soaking a polymeric powder with a suitably large amount of an acid solution which causes the polymer to dissolve and form a matrix having a gel-like or paste-like consistency at room temperature.
  • suitably large amount of acid is meant between about 70% to about 99.9%, by weight, of the polymer-acid solution mixture which forms the paste or gel.
  • the polymer is PBI.
  • PBI is currently preferred because the inventors have found that the basic nature of the PBI polymer causes it to have an affinity for acids, which permits it to retain the acids under extreme conditions.
  • other suitable polymers e.g., polyaniline and polypyrimidine which swell upon mixture with the acid solutions described herein and form a paste- or gel-like matrix of the invention.
  • PBI polymers, as well as other polymers useful in the invention are readily obtained by one of skill in the art.
  • other polymeric materials permit production of gel or paste-like matrix of the invention having variances in acid content within the ranges provided herein.
  • An acid solution useful for addition to the polymer may contain approximately 100% acid, or may contain a suitable acid diluted by or dissolved in a suitable solvent.
  • the acid solution desirably contains between about 5 weight percent (wt %) to about 100 wt% of an acid and up to about 95 wt% solvent.
  • the acid solution contains about 85 wt% acid and 15 wt% water or methanol.
  • Suitable acids may include, for example, acetic acid, formic acid, nitric acid, hydrochloric acid, phosphoric acid, sulfuric acid, trifluoroacetic acid, triflic acid and mixtures of these acids or mixtures of these acids and phosphoric acid.
  • the preferred acid is phosphoric acid.
  • any other suitable acid may readily select any other suitable acid.
  • the present invention is not limited to the choice of suitable acid, provided that the acid swells the polymer, e.g., PBI, and permits the formation of a matrix.
  • the most preferred acid solution contains about 85% by weight phosphoric acid and 15% by weight water.
  • other suitable acid solution concentrations using other selected acids may be readily determined and selected by one of skill in the art.
  • the polymer and acid solution may be combined and mixed at room temperature. However, any temperature between the freezing point and boiling point of the acid may be used.
  • the mixture is heated to enable it to reach a gel-like or paste-like consistency more rapidly than at room temperature. Desirably, the mixture is heated to between about 50°C to about 200°C, and more preferably to between about 100° to about 150°C. Suitably, the heating step is performed for between about five minutes to about four hours, and more preferably for about one hour.
  • the paste or gel matrix of the invention forms.
  • the present invention provides a PBI paste or gel.
  • the resulting PBI paste or gel is characterized by containing between 70 - 99.9% acid, and preferably about 99% acid, by weight.
  • Such a paste or gel is characterized by higher acid loadings and improved electrochemical properties compared to other compositions of the prior art for the same use.
  • the PBI paste or gel of this invention may be characterized by better retention of the acid than the pastes or gels of the prior art (e.g. phosphoric acid and silicon carbide pastes) .
  • the PBI paste or gel of the invention is useful for a variety of purposes, and particularly in coating such materials as fabrics and films.
  • the coated fabrics, and films, as well as the paste or gel are useful in fuel cells. Desirably, where the paste or gel of the invention is used in fuel cells, it is produced by mixing the polymer and acid, as described above .
  • the present invention provides a fabric or film coated with a PBI paste or gel of the invention.
  • Suitable fabrics and films are desirably polymeric.
  • the fabric or film is derived from polymers including, but not limited to, polybenzimidazole (PBI) and derivatives thereof, poly (pyridine) , poly (pyrimidine) , polyimidazoles, polybenzthiazoles, polybenzoxazoles, polyoxadiazoles, polyquinoxalines, polythiadiazoles, and poly (tetrazapyrenes) .
  • PBI polybenzimidazole
  • the selected polymeric fabric or film is provided with a coating of between 0.1 to 50 ⁇ M of the paste or gel.
  • the coating is applied using conventional means, such as roll coating, knife coating, Gravure coating, brush coating, spray coating, dip coating and other known techniques. General descriptions of these types of coating methods may be found in texts, such as Modern Coa ting and Drying Techniques, (E. Cohen and E. Gutoff, eds; VCH Publishers) New York (1992) and Web Processing and Converting Technology and Equipment, (D. Satas, ed; Van Nostrand Reinhold) New York (1984).
  • the manner of coating the fabric or film is not a limitation of this invention.
  • a fabric of the invention is imbibed with acid according to the method described in the co- pending, co-filed US patent application for "Process for Producing Polybenzimidazole Fabrics for Use in Fuel Cells", which is incorporated by reference.
  • acid-imbibed fabric disclosed in that application contains between about 40 to about 95% acid, by weight, and more preferably about 50 to about 75% acid, by weight, of the imbibed fabric.
  • a fabric containing polymeric fiber is utilized to prepare the acid-imbibed fabric.
  • polystyrene resin examples include, but are not limited to, polybenzimidazole (PBI), poly (pyridine) , poly (pyrimidine) , polyimidazoles, polybenzthiazoles, polybenzoxazoles, polyoxadiazoles, polyquinoxalines, polythiadiazoles, poly (tetrazapyrenes) , and mixtures of sulfonated, non-sulfonated PBI and/or such polymeric fibers.
  • PBI polybenzimidazole
  • poly (pyridine) poly (pyrimidine)
  • polyimidazoles polybenzthiazoles
  • polybenzoxazoles polyoxadiazoles
  • polyquinoxalines polythiadiazoles
  • poly (tetrazapyrenes) examples include, but are not limited to, polybenzimidazole (PBI), poly (pyridine) , poly (pyrimidine) , polyimidazoles, polybenzthiazoles, polybenzoxazoles, polyo
  • knitted or non-woven fabrics which contain voids which permit imbibition of the acid, as described herein, may also be utilized.
  • the fabric is imbibed with acid by soaking it in an appropriate acid solution, optionally in the presence of heat.
  • an appropriate acid solution optionally in the presence of heat.
  • the present invention provides a polymeric film coated with a PBI paste or gel of the invention as described above, and joined or place adjacent to a second polymeric film, thereby forming a sandwich structure.
  • the coated fabric or film of the invention is useful, for example, as the polymer electrolyte in a fuel cell of the invention.
  • the invention provides a method of preparing an electrode for use in a fuel cell by coating an electrode with a PBI paste and gel of the invention as described above. Another advantage of this invention is that the PBI paste or gel of the invention is more readily applied to the electrode material than are prior art electrolytes.
  • the invention further provides fuel cells containing the electrodes, fabrics, and films coated with the PBI paste or gel according to the invention.
  • An exemplary PBI paste of this invention is prepared as follows. Commercially available PBI polymer (lg) was added to a solution containing 117 g 85% H 3 P0 4 and 15%, by weight, water in a slow mixer. The mixture is agitated at a temperature of 100-150°C to remove residual water until a consistent paste is obtained. The resulting paste or gel contains about 99% acid by weight.
  • PBI paste is prepared as follows. PBI polymer (5g) was added to a solution containing 112 g 85% HP0 and 15%, by weight, water in a slow mixer. The mixture is agitated at a temperature of 100-150°C to remove residual water until a consistent paste is obtained. The resulting paste or gel contains about 96% acid by weight.
  • Example 3 PBI gel prepared from Example 1 was slot-coated at room temperature onto a phosphoric acid imbibed PBI fabric. The thickness of the coating was about 25 ⁇ m. A similar coating was applied to a platinum electrode.
  • a membrane electrode assembly was assembled from these materials and a second electrode such that the layers were ordered electrode/gel/fabric/gel/electrode.
  • Example 3 The membrane electrode assembly fashioned in Example 3 was then placed in a fuel cell. Under typical operating conditions at 0.7 volts the resulting current density and power density is approximately 450 milliamperes/cm 2 and 315 milliwatts/cm 2 , respectively. Numerous modifications and variations of the present invention are included in the above-identified specification and are expected to be obvious to one of skill in the art. Such modifications and alterations to the compositions and processes of the present invention are believed to be encompassed in the scope of the claims appended hereto.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Electrochemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Dispersion Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Composite Materials (AREA)
  • Fuel Cell (AREA)
  • Macromolecular Compounds Obtained By Forming Nitrogen-Containing Linkages In General (AREA)
  • Inert Electrodes (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

A method for producing polybenzimidazole (PBI) paste or gel useful in a fuel cell, mixing PBI polymer powder with a suitable amount of an acid, which permits the polymer to dissolve and form a matrix having a gel-like or paste-like consistency at room temperature.

Description

PROCESS FOR PRODUCING POLYBENZIMIDAZOLE PASTES AND GELS FOR USE IN FUEL CELLS
Field of the Invention
This invention relates to the manufacture of a paste or gel for use as a polymer electrolyte in fuel cell applications.
Background of the Invention
Fuel cells can be configured in numerous ways with a variety of electrolytes, fuels and operating temperatures. For example, fuels such as hydrogen or methanol can be provided directly to the fuel cell electrode. Alternatively, fuels, such as methane or methanol, can be converted to a hydrogen rich gas mixture external to the cell itself and subsequently provided to the fuel cell. Air is the source of oxygen in most fuel cells, although in some applications, the oxygen is obtained by hydrogen peroxide decomposition or from a cryogenic storage system.
Although there are theoretically a limitless number of combinations of electrolyte, fuel, oxidant, temperatures and so on, practical systems include solid polymer electrolyte systems using hydrogen or hydrazine as the fuel source and pure oxygen as the oxidant. Polybenzimidazole (PBI) which has been doped with a strong acid is an example of a suitable solid polymer for use in an electrolyte system.
It is known in the art to imbibe polybenzimidazole (PBI) dense films with a strong acid to make a proton conducting media. Particularly, United States Patent No. 5,525,436, issued June 11, 1996, described a method of doping PBI film with a strong acid, such as phosphoric acid or sulfuric acid, such that a single phase system is formed, i.e., acid is dissolved in the polymer.
Even in view of the advances in the art, the performance, high cost and processability of suitable polymeric electrolyte materials remain important considerations in fuel cell construction with respect to polymeric media for fuel cells. There remains a need in the art for new materials for use in fuel cells.
Summary of the Invention In one aspect, the present invention provides a method of preparing a polymeric, preferably PBI, paste or gel for use as an electrolyte in fuel cells. In one embodiment, the method comprises soaking finely divided
PBI polymer in a suitable amount of an acid solution which permits the polymer to dissolve and form a matrix having a gel-like or paste-like consistency at room temperature.
In another aspect, the present invention provides a PBI paste or gel, which contains between about 70 to about 99.9% by weight of imbibed acid, which paste or gel is useful in fuel cells. These pastes or gels are prepared by the methods described herein.
In still another aspect, the invention provides a polymeric fabric coated with a PBI paste or gel according to the invention.
In yet another aspect, the invention provides a fuel cell comprising a PBI paste or gel, or coated fabric, according to this invention. In a further aspect, the present invention provides a polymeric film coated with a PBI paste or gel of the invention.
In a further aspect, the present invention provides a polymeric film coated with a PBI paste or gel of the invention with a second polymeric film forming a sandwich structure.
In still a further aspect, the present invention provides a method for preparing an electrode for use in fuel cells by steps which include coating the electrode with a paste or gel of the invention.
Other aspects and advantages of the present invention are described further in the following detailed description of the preferred embodiments thereof.
Detailed Description of the Invention
The present invention provides an improvement over the art in methods of preparing a polymeric paste or gel which contains acid and is useful as an electrolyte in fuel cells, particularly chlorine-resistant fuel cells, and in the preparation of adhesives. Also provided are the pastes or gels prepared by the method of the invention, as well as fabric and film coated thereby, and fuel cells containing the pastes or gels of the invention.
Generally, according to the process of the invention, a polymeric paste or gel is prepared by mixing or soaking a polymeric powder with a suitably large amount of an acid solution which causes the polymer to dissolve and form a matrix having a gel-like or paste-like consistency at room temperature. By "suitably large amount of acid" is meant between about 70% to about 99.9%, by weight, of the polymer-acid solution mixture which forms the paste or gel.
Preferably, the polymer is PBI. PBI is currently preferred because the inventors have found that the basic nature of the PBI polymer causes it to have an affinity for acids, which permits it to retain the acids under extreme conditions. However, one of skill in the art can readily determine other suitable polymers , and desirably, other basic polymers such as e.g., polyaniline and polypyrimidine which swell upon mixture with the acid solutions described herein and form a paste- or gel-like matrix of the invention. These PBI polymers, as well as other polymers useful in the invention, are readily obtained by one of skill in the art. Similarly, other polymeric materials permit production of gel or paste-like matrix of the invention having variances in acid content within the ranges provided herein.
An acid solution useful for addition to the polymer may contain approximately 100% acid, or may contain a suitable acid diluted by or dissolved in a suitable solvent. For example, the acid solution desirably contains between about 5 weight percent (wt %) to about 100 wt% of an acid and up to about 95 wt% solvent. In a currently preferred embodiment, the acid solution contains about 85 wt% acid and 15 wt% water or methanol. Suitable acids may include, for example, acetic acid, formic acid, nitric acid, hydrochloric acid, phosphoric acid, sulfuric acid, trifluoroacetic acid, triflic acid and mixtures of these acids or mixtures of these acids and phosphoric acid. Currently, the preferred acid is phosphoric acid. However, one of skill in the art may readily select any other suitable acid. The present invention is not limited to the choice of suitable acid, provided that the acid swells the polymer, e.g., PBI, and permits the formation of a matrix. Currently, the most preferred acid solution contains about 85% by weight phosphoric acid and 15% by weight water. However, as stated above, other suitable acid solution concentrations using other selected acids may be readily determined and selected by one of skill in the art.
The polymer and acid solution may be combined and mixed at room temperature. However, any temperature between the freezing point and boiling point of the acid may be used. Optionally, the mixture is heated to enable it to reach a gel-like or paste-like consistency more rapidly than at room temperature. Desirably, the mixture is heated to between about 50°C to about 200°C, and more preferably to between about 100° to about 150°C. Suitably, the heating step is performed for between about five minutes to about four hours, and more preferably for about one hour. Upon cooling, the paste or gel matrix of the invention forms.
Thus, the present invention provides a PBI paste or gel. The resulting PBI paste or gel is characterized by containing between 70 - 99.9% acid, and preferably about 99% acid, by weight. Such a paste or gel is characterized by higher acid loadings and improved electrochemical properties compared to other compositions of the prior art for the same use. For example, the PBI paste or gel of this invention may be characterized by better retention of the acid than the pastes or gels of the prior art (e.g. phosphoric acid and silicon carbide pastes) . The PBI paste or gel of the invention is useful for a variety of purposes, and particularly in coating such materials as fabrics and films. The coated fabrics, and films, as well as the paste or gel, are useful in fuel cells. Desirably, where the paste or gel of the invention is used in fuel cells, it is produced by mixing the polymer and acid, as described above .
Thus, as another aspect, the present invention provides a fabric or film coated with a PBI paste or gel of the invention. Suitable fabrics and films are desirably polymeric. Desirably, the fabric or film is derived from polymers including, but not limited to, polybenzimidazole (PBI) and derivatives thereof, poly (pyridine) , poly (pyrimidine) , polyimidazoles, polybenzthiazoles, polybenzoxazoles, polyoxadiazoles, polyquinoxalines, polythiadiazoles, and poly (tetrazapyrenes) . The presently preferred, and exemplified polymer, is PBI. Once the selected fabric or film is coated according to the invention, it is particularly well suited for use in a fuel cell. These coated fabrics and films may be produced using methods well known to those of skill in the art.
Desirably, the selected polymeric fabric or film is provided with a coating of between 0.1 to 50 μM of the paste or gel. The coating is applied using conventional means, such as roll coating, knife coating, Gravure coating, brush coating, spray coating, dip coating and other known techniques. General descriptions of these types of coating methods may be found in texts, such as Modern Coa ting and Drying Techniques, (E. Cohen and E. Gutoff, eds; VCH Publishers) New York (1992) and Web Processing and Converting Technology and Equipment, (D. Satas, ed; Van Nostrand Reinhold) New York (1984). The manner of coating the fabric or film is not a limitation of this invention. Alternatively, in one particularly desired embodiment, a fabric of the invention is imbibed with acid according to the method described in the co- pending, co-filed US patent application for "Process for Producing Polybenzimidazole Fabrics for Use in Fuel Cells", which is incorporated by reference. Briefly, acid-imbibed fabric disclosed in that application contains between about 40 to about 95% acid, by weight, and more preferably about 50 to about 75% acid, by weight, of the imbibed fabric. A fabric containing polymeric fiber is utilized to prepare the acid-imbibed fabric. Examples of such polymers include, but are not limited to, polybenzimidazole (PBI), poly (pyridine) , poly (pyrimidine) , polyimidazoles, polybenzthiazoles, polybenzoxazoles, polyoxadiazoles, polyquinoxalines, polythiadiazoles, poly (tetrazapyrenes) , and mixtures of sulfonated, non-sulfonated PBI and/or such polymeric fibers. Currently, the preferred fiber is a PBI fiber, which may be either sulfonated or non-sulfonated. Suitable fabrics are readily available from a variety of commercial sources, and are preferably woven and contain voids between the individual fibers in the fabric. However, knitted or non-woven fabrics which contain voids which permit imbibition of the acid, as described herein, may also be utilized. The fabric is imbibed with acid by soaking it in an appropriate acid solution, optionally in the presence of heat. A more detailed description of the acid-imbibed fabric and its production are provided in the above-reference patent application.
In a further aspect, the present invention provides a polymeric film coated with a PBI paste or gel of the invention as described above, and joined or place adjacent to a second polymeric film, thereby forming a sandwich structure.
The coated fabric or film of the invention, including the "film sandwich" described above, is useful, for example, as the polymer electrolyte in a fuel cell of the invention. Thus, in another embodiment, the invention provides a method of preparing an electrode for use in a fuel cell by coating an electrode with a PBI paste and gel of the invention as described above. Another advantage of this invention is that the PBI paste or gel of the invention is more readily applied to the electrode material than are prior art electrolytes. The invention further provides fuel cells containing the electrodes, fabrics, and films coated with the PBI paste or gel according to the invention.
The following examples illustrate the preferred compositions and methods of the invention, using PBI as the exemplified polymer. These examples are illustrative only and do not limit the scope of the invention.
Example 1
An exemplary PBI paste of this invention is prepared as follows. Commercially available PBI polymer (lg) was added to a solution containing 117 g 85% H3P04 and 15%, by weight, water in a slow mixer. The mixture is agitated at a temperature of 100-150°C to remove residual water until a consistent paste is obtained. The resulting paste or gel contains about 99% acid by weight.
Example 2
Another exemplary PBI paste is prepared as follows. PBI polymer (5g) was added to a solution containing 112 g 85% HP0 and 15%, by weight, water in a slow mixer. The mixture is agitated at a temperature of 100-150°C to remove residual water until a consistent paste is obtained. The resulting paste or gel contains about 96% acid by weight.
Example 3 PBI gel prepared from Example 1 was slot-coated at room temperature onto a phosphoric acid imbibed PBI fabric. The thickness of the coating was about 25 μm. A similar coating was applied to a platinum electrode.
A membrane electrode assembly was assembled from these materials and a second electrode such that the layers were ordered electrode/gel/fabric/gel/electrode.
Example 4
The membrane electrode assembly fashioned in Example 3 was then placed in a fuel cell. Under typical operating conditions at 0.7 volts the resulting current density and power density is approximately 450 milliamperes/cm2 and 315 milliwatts/cm2, respectively. Numerous modifications and variations of the present invention are included in the above-identified specification and are expected to be obvious to one of skill in the art. Such modifications and alterations to the compositions and processes of the present invention are believed to be encompassed in the scope of the claims appended hereto.

Claims

WHAT IS CLAIMED IS:
1. A method for producing a polybenzimidazole (PBI) paste or gel comprising mixing a polymeric PBI powder with a suitable amount of an acid solution, which permits the polymer to dissolve and form a matrix having a gel-like or paste-like consistency at room temperature .
2. The method according to claim 1 further comprising heating said mixture.
3. The method according to claim 1 wherein said acid solution comprises an acid and a solvent selected from the group consisting of water or methanol.
4. The method according to claim 3, wherein said acid is present in solution at between 5% by weight to about 100% by weight of said solution.
5. The method according to claim 4, wherein said solvent is present in said solution at between about 0 and about 5% by weight of said solution.
6. The method according to claim 1, wherein said acid is selected from the group consisting of phosphoric acid, acetic acid, formic acid, nitric acid, hydrochloric acid, sulfuric acid, methanesulfonic acid, trifluoroacetic acid, triflic acid and mixtures thereof.
7. The method according to claim 3, wherein the suitable amount of said acid solution is between about 70 to about 99.9% of the total weight of said paste or gel mixture.
8. The method according to claim 7, wherein the suitable amount of said solution is between about 95 to about 99% of the total weight of said paste or gel mixture .
9. The method according to claim 7, wherein the amount of said PBI in said paste or gel is between about 0.1% to about 30% by weight of said paste or gel mixture .
10. The method according to claim 2 wherein said mixture is heated to between about 50 to 200┬░C for a time sufficient for the mixture to form a paste or gel.
11. The method according to claim 10 wherein said time is between 5 minutes to 4 hours.
12. A PBI paste or gel comprising a phosphoric acid solution content of between about 70 to 99.9% by weight and about 0.01 to about 30% by weight, PBI, of the total weight of said paste or gel.
13. A PBI paste or gel produced according to claims 1-11.
14. A fuel cell comprising a paste or gel, which comprises a phosphoric acid solution content of between about 70 to 99.9% by weight and about 0.01 to about 30% by weight, PBI, of the total weight of said paste or gel.
15. A polymeric fabric or film coated with a paste or gel, which comprises a phosphoric acid solution content of between about 70 to 99.9% by weight and about 0.01 to about 30% by weight, PBI, of the total weight of said paste or gel.
16. The fabric according to claim 15, which has been imbibed with acid prior to coating with said paste or gel.
17. A fuel cell comprising a fabric coated with a paste or gel, which comprises a phosphoric acid solution content of between about 70 to 99.9% by weight and about 0.01 to about 30% by weight, PBI, of the total weight of said paste or gel.
18. A polymeric film coated with a paste or gel, which comprises a phosphoric acid solution content of between about 70 to 99.9% by weight and about 0.01 to about 30% by weight, PBI, of the total weight of said paste or gel.
19. A method of preparing an electrode for use in fuel cells comprising coating said electrode with a paste or gel which comprises a phosphoric acid solution content of between about 70 to 99.9% by weight and about 0.01 to about 30% by weight, PBI, of the total weight of said paste or gel.
PCT/US1998/010464 1997-07-16 1998-05-18 Process for producing polybenzimidazole pastes and gels for use in fuel cells WO1999004445A1 (en)

Priority Applications (9)

Application Number Priority Date Filing Date Title
EP98924836A EP0996990B1 (en) 1997-07-16 1998-05-18 Process for producing polybenzimidazole pastes and gels for use in fuel cells
KR20007000460A KR100511152B1 (en) 1997-07-16 1998-05-18 Process for producing polybenzimidazole pastes and gels for use in fuel cells
DK98924836T DK0996990T3 (en) 1997-07-16 1998-05-18 Process for the preparation of polybenzimidazole pastes and gels for use in fuel cells
CA002306481A CA2306481C (en) 1997-07-16 1998-05-18 Process for producing polybenzimidazole pastes and gels for use in fuel cells
BR9811508-1A BR9811508A (en) 1997-07-16 1998-05-18 "process for producing polybenzimidazole pastes and gels for use in fuel cells"
AU76914/98A AU7691498A (en) 1997-07-16 1998-05-18 Process for producing polybenzimidazole pastes and gels for use in fuel cells
JP2000503566A JP4754687B2 (en) 1997-07-16 1998-05-18 Process for producing polybenzimidazole pastes and gels for use in fuel cells
AT98924836T ATE251805T1 (en) 1997-07-16 1998-05-18 METHOD FOR PRODUCING POLYBENZIMIDAZOLE PASTES AND GELS FOR USE IN FUEL CELLS
DE69818826T DE69818826T2 (en) 1997-07-16 1998-05-18 METHOD FOR PRODUCING POLYBENZIMIDAZOLE PASTES AND GELS FOR USE IN FUEL CELLS

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US08/895,059 US5945233A (en) 1997-07-16 1997-07-16 Process for producing polybenzimidazole pastes and gels for use in fuel cells
US08/895,059 1997-07-16

Publications (1)

Publication Number Publication Date
WO1999004445A1 true WO1999004445A1 (en) 1999-01-28

Family

ID=25403892

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US1998/010464 WO1999004445A1 (en) 1997-07-16 1998-05-18 Process for producing polybenzimidazole pastes and gels for use in fuel cells

Country Status (13)

Country Link
US (1) US5945233A (en)
EP (1) EP0996990B1 (en)
JP (1) JP4754687B2 (en)
KR (1) KR100511152B1 (en)
CN (1) CN100377410C (en)
AT (1) ATE251805T1 (en)
AU (1) AU7691498A (en)
BR (1) BR9811508A (en)
CA (1) CA2306481C (en)
DE (1) DE69818826T2 (en)
DK (1) DK0996990T3 (en)
TW (1) TW432743B (en)
WO (1) WO1999004445A1 (en)

Cited By (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001018894A2 (en) * 1999-09-09 2001-03-15 Danish Power Systems Aps Polymer electrolyte membrane fuel cells
DE102006062251A1 (en) * 2006-12-22 2008-06-26 Volkswagen Ag Membrane electrode unit for high temperature gas cell, comprises polymer membrane impregnated with electrolytes, and cathodic- and anodic gas diffusion electrodes placed at cathode- and anode lateral membrane surfaces respectively
DE102007002515A1 (en) 2007-01-17 2008-08-14 Volkswagen Ag Polymer electrolyte membrane useful for high temperature-fuel cell for traction systems or the additional power supply of motor vehicles, comprises an organic polymer material impregnated with an electrolyte, and a laminated structure
DE102007018280A1 (en) 2007-04-18 2008-10-23 Volkswagen Ag Polymer electrolyte membrane manufacturing method for fuel cell, involves impregnating polymer membrane with liquid or solved electrolytes, where polymer membrane is supported between carrier foils that lie at both sides of polymer membrane
DE102007020947A1 (en) 2007-05-04 2008-11-13 Volkswagen Ag Gas diffusion electrode for fuel cell, particularly for high temperature fuel cells based on electrolyte impregnated membranes, has gas diffusion layer and porous catalyst layer arranged on gas diffusion layer
DE102007025207A1 (en) 2007-05-30 2008-12-04 Volkswagen Ag Gas diffusion electrode for high temperature gas cells based on electrolyte-impregnated membrane, comprises gas diffusion layer, and porous catalyst layer arranged on diffusion layer and having conductive substrate and catalytic material
DE102007031280A1 (en) 2007-07-05 2009-01-08 Volkswagen Ag Gas diffusion electrode with membrane-electrode-unit for high temperature fuel cells based on membrane for traction system, has gas diffusion layer and catalyst layer is impregnated with another electrolyte and has hydrophobic material
DE102007044246A1 (en) 2007-09-11 2009-03-12 Volkswagen Ag Membrane electrode unit with hydrogenatable material for a fuel cell
DE102007061061A1 (en) 2007-12-14 2009-06-18 Volkswagen Ag Fuel cell stack for traction system of motor vehicle, has hydrogen supply line for supplying hydrogen to anodes and dummy cell, and hydrogen discharge line for removing residual hydrogen from anode and dummy cell
KR100905688B1 (en) * 2001-09-12 2009-07-03 바스프 푸엘 셀 게엠베하 Proton-conducting membrane and the use of the same
DE102008009437A1 (en) 2008-02-14 2009-09-03 Volkswagen Ag Membrane-electrode unit for high temperature-proton exchange membrane-fuel cell, has polymer electrolyte membrane with polymer membrane impregnated with electrolyte
DE102008019874A1 (en) 2008-04-17 2009-10-22 Volkswagen Ag Method for determining content or partial pressure of gas component in gas mixture of fuel cell, involves detecting sound velocity of gas mixture, where content or partial pressure is determined in dependence of sound velocity
DE102008041225A1 (en) 2008-08-13 2010-02-18 Volkswagen Ag Fuel cell for supplying electricity to e.g. drive motor of motor vehicle, has discharging systems arranged in fuel cell stack that is upstream in hydrogen flow direction and connected with supply systems of downstream fuel cell stack
DE102009001137A1 (en) 2008-10-29 2010-05-06 Volkswagen Ag Polymer electrolyte membrane for fuel cells, comprises a polymer component, an electrolyte mixture, and additive components for increasing proton conductivity of the membrane and for influencing its mechanical- and/or surfaces properties
DE102009001141A1 (en) 2008-10-29 2010-05-06 Volkswagen Ag Producing polymer electrolyte membrane, by producing polymer solution of polyazol in solvent mixture, transferring polymer solution in flat structure, and dropping polymer solution that is transferred in flat structure with liquid water
DE102009028308A1 (en) 2009-08-06 2011-02-10 Volkswagen Ag Membrane electrode unit, useful in fuel cell, comprises a polymer electrolyte membrane made of a polymer, two electrodes sandwiching polymer electrolyte membrane, an electrolyte wetting polymer electrolyte membrane and silicate derivative
WO2011020872A1 (en) 2009-08-20 2011-02-24 Volkswagen Ag Long-term stable polymer electrolyte membrane for ht fuel cells and method for the production thereof
WO2010145827A3 (en) * 2009-06-20 2011-03-10 Basf Se Composition containing polyazole
WO2010145828A3 (en) * 2009-06-20 2011-03-10 Basf Se Method for the production of a high-molecular polyazole
DE102009057797A1 (en) 2009-12-10 2011-06-16 Volkswagen Ag Method for producing a catalytic material for electrodes of a fuel cell
EP2424026A1 (en) * 2010-08-31 2012-02-29 Aisin Seiki Kabushiki Kaisha Fuel cell electrolyte membrane, membrane electrode assembly, fuel cell and method of manufacturing fuel cell electrolyte membrane

Families Citing this family (31)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6042968A (en) * 1997-07-16 2000-03-28 Aventis Research & Technologies Gmbh & Co. Kg Process for producing polybenzimidazole fabrics for use in fuel
US6492044B1 (en) 2000-06-29 2002-12-10 Plug Power Inc. Reactant conditioning for high temperature fuel cells
DE10155543C2 (en) * 2001-11-12 2003-11-13 Sartorius Gmbh Proton-conducting electrolyte membrane, process for its production and its use
CN100388552C (en) * 2001-11-12 2008-05-14 赛多利斯司特蒂姆生物工艺公司 Proton-conducting electrolyte membrane, method for production and use thereof in a fuel cell
EP1680831A2 (en) * 2003-10-10 2006-07-19 Ballard Power Systems Inc. Water insoluble additive for improving conductivity of an ion exchange membrane
KR100570745B1 (en) * 2003-10-30 2006-04-12 삼성에스디아이 주식회사 A method for preparing poly2,5-benzimidazole
JP5005160B2 (en) * 2003-12-08 2012-08-22 三星エスディアイ株式会社 Gel electrolyte and fuel cell
US7115334B2 (en) * 2003-12-08 2006-10-03 Samsung Sdi Co., Ltd. Gel electrolyte and fuel cell employing the same
US7259230B2 (en) * 2004-06-07 2007-08-21 Battelle Energy Alliance, Llc Polybenzimidazole compounds, polymeric media, and methods of post-polymerization modifications
US7309758B2 (en) 2004-06-07 2007-12-18 Battelle Energy Alliance, Llc Polybenzimidazole compounds, polymeric media, and methods of post-polymerization modifications
KR100542203B1 (en) * 2004-06-30 2006-01-10 삼성에스디아이 주식회사 Binder solution for fuel cell, membrane electrode assemblymea for fuel cell, and method for preparating the membrane electrode assembly
FR2876531A1 (en) * 2004-10-07 2006-04-14 Nextamp Sa TATTOO READING METHOD AND DEVICE, COMPUTER PROGRAM PRODUCT, AND STORAGE MEDIUM
KR100738788B1 (en) * 2004-12-07 2007-07-12 주식회사 엘지화학 Polybenzimidazole-benzamide copolymer, process for preparing the same, electrolyte membrane prepared therefrom and process for preparing the same
CN100336861C (en) * 2004-12-30 2007-09-12 同济大学 Electric conducting mateiral of non-water proton of polyvinyl alcohol tetrazole with acid being adulterated and preparation method
EP1760110B1 (en) 2005-09-03 2011-11-02 Samsung SDI Co., Ltd. Polybenzoxazine-based compound, electrolyte membrane including the same, and fuel cell employing the electrolyte membrane
KR100819676B1 (en) 2005-11-14 2008-04-03 주식회사 엘지화학 Branched multiblock polybenzimidazole-benzamide copolymer and method for preparing the same, electrolyte membrane and paste/gel prepared therefrom
US7977392B2 (en) * 2005-12-22 2011-07-12 Daimler Ag Water insoluble additive for improving conductivity of an ion exchange membrane
CN100395289C (en) * 2006-04-27 2008-06-18 同济大学 Non-aqueous proton conducting material based on imidazole oligomer and preparation process thereof
CN100400597C (en) * 2006-04-27 2008-07-09 同济大学 High anti ehcmical oxidizing polymer based on aza-cycle component
KR100818255B1 (en) 2006-05-29 2008-04-02 삼성에스디아이 주식회사 Polybenzoxazines, an electrolyte membrane comprising the same and fuel cell employing the electrolyte membrane
KR100745741B1 (en) * 2006-08-22 2007-08-02 삼성에스디아이 주식회사 Membrane and electrode assembly for fuel cell and fuel cell employing the same
US20080317946A1 (en) * 2007-06-21 2008-12-25 Clearedge Power, Inc. Fuel cell membranes, gels, and methods of fabrication
EP2036910B1 (en) 2007-09-11 2012-06-27 Samsung Electronics Co., Ltd. Benzoxazine-based monomer, polymer thereof, electrode for fuel cell including the same, electrolyte membrane for fuel cell includind the same, and fuel cell using the same
EP2433947B1 (en) * 2007-09-11 2014-05-07 Samsung Electronics Co., Ltd. Phosphorous containing benzoxazine-based monomer
KR101366808B1 (en) * 2007-10-11 2014-02-25 삼성전자주식회사 Polybenzimidazole-base complex, crosslinked material of polybenzoxazines formed thereof, and fuel cell using the same
EP2055706B1 (en) * 2007-11-02 2011-08-24 Samsung Electronics Co., Ltd. Electrode and electrolyte membrane for fuel cell including a naphthoxazine based polymer and fuel cell using the electrode
EP2058321B1 (en) 2007-11-02 2014-01-08 Samsung Electronics Co., Ltd. Phosphorous containing monomer, polymer thereof, electrode for fuel cell including the polymer, electrolyte membrane for fuel cell including the polymer, and fuel cell using the electrode
KR101537311B1 (en) * 2007-11-02 2015-07-17 삼성전자주식회사 Electrolyte Membrane for fuel cell and fuel cell using the same
EP2062891B1 (en) * 2007-11-06 2012-08-08 Samsung Electronics Co., Ltd. Benzoxazine-based monomer, polymer thereof, electrode for fuel cell including the polymer, electrolyte membrane for fuel cell including the polymer, and fuel cell using the electrode
DK180360B1 (en) 2019-08-14 2021-02-04 Blue World Technologies Holding ApS Method of producing separator plates by compaction and a production facility
DK180599B1 (en) 2020-01-20 2021-10-14 Blue World Technologies Holding ApS Apparatus and process for making acid-doped proton exchange membranes

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4945156A (en) * 1988-12-29 1990-07-31 Honeywell Inc. Solution processing of rigid chain and ladder polymers
WO1992010527A1 (en) * 1990-12-07 1992-06-25 The Dow Chemical Company Process for fabricating oriented polybenzazole films
WO1996013872A1 (en) * 1994-11-01 1996-05-09 Case Western Reserve University Proton conducting polymers
US5599639A (en) * 1995-08-31 1997-02-04 Hoechst Celanese Corporation Acid-modified polybenzimidazole fuel cell elements
WO1997023919A1 (en) * 1995-12-22 1997-07-03 Hoechst Research & Technology Deutschland Gmbh & Co.Kg Process for continuous production of membrane-electrode composites
US5693434A (en) * 1996-07-22 1997-12-02 Motorola, Inc. Electrochemical cell having a polymer electrolyte

Family Cites Families (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1545012A1 (en) * 1962-11-19 1969-07-24 Whittaker Corp Meltable condensation polymers, their use and processes for their preparation
US4309372A (en) * 1977-03-10 1982-01-05 The United States Of America As Represented By The Administrator Of The National Aeronautics And Space Administration Method of making formulated plastic separators for soluble electrode cells
US4448687A (en) * 1982-12-17 1984-05-15 Celanese Corporation Process for the production of semipermeable polybenzimidazole membranes with low temperature annealing
US4693824A (en) * 1985-09-23 1987-09-15 Celanese Corporation Process for the production of polybenzimidazole ultrafiltration membranes
US4598099A (en) * 1985-10-24 1986-07-01 Celanese Corporation Process for the production of polybenzimidazole foams
US4664761A (en) * 1985-12-27 1987-05-12 Uop Inc. Electrochemical method and apparatus using proton-conducting polymers
US4868008A (en) * 1986-10-23 1989-09-19 Hoechst Celanese Corp. Process for preparing electrically conductive shaped articles from polybenzimidazoles
US4814399A (en) * 1987-07-24 1989-03-21 Hoechst Celanese Corporation Sulfoalkylation of polybenzimidazole
US4927909A (en) * 1987-09-18 1990-05-22 Hoechst Celanese Corp. Fabrication of high performance polybenzimidazole films
US5091087A (en) * 1990-06-25 1992-02-25 Hoechst Celanese Corp. Fabrication of microporous PBI membranes with narrow pore size distribution
US5264542A (en) * 1992-05-27 1993-11-23 Hoechst Celanese Corp. Process for preparing stabilized polybenzimidazole products
US5277981A (en) * 1992-05-28 1994-01-11 Hoechst Celanese Corp. Thermo-oxidatively stabilized polybenzimidazole-containing articles
EP0604883A3 (en) * 1992-12-30 1995-02-15 Hoechst Ag Process for preparing porous hydrophilic membranes.
US5292469A (en) * 1993-01-05 1994-03-08 The Dow Chemical Company Process for coagulation, washing and leaching of shaped polybenzazole articles
EP0954544B1 (en) * 1996-10-01 2002-03-27 Celanese Ventures GmbH Process for producing polymeric films for use as fuel cells
US5723231A (en) * 1996-12-09 1998-03-03 Motorola, Inc. Polymer electrolyte and an electrochemical cell containing the electrolyte
JP4398522B2 (en) * 1997-05-22 2010-01-13 バスフ・ヒュエル・セル・ゲーエムベーハー Method for producing polymer electrolyte membrane for fuel cell and fuel cell

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4945156A (en) * 1988-12-29 1990-07-31 Honeywell Inc. Solution processing of rigid chain and ladder polymers
WO1992010527A1 (en) * 1990-12-07 1992-06-25 The Dow Chemical Company Process for fabricating oriented polybenzazole films
WO1996013872A1 (en) * 1994-11-01 1996-05-09 Case Western Reserve University Proton conducting polymers
US5525436A (en) * 1994-11-01 1996-06-11 Case Western Reserve University Proton conducting polymers used as membranes
US5599639A (en) * 1995-08-31 1997-02-04 Hoechst Celanese Corporation Acid-modified polybenzimidazole fuel cell elements
WO1997023919A1 (en) * 1995-12-22 1997-07-03 Hoechst Research & Technology Deutschland Gmbh & Co.Kg Process for continuous production of membrane-electrode composites
US5693434A (en) * 1996-07-22 1997-12-02 Motorola, Inc. Electrochemical cell having a polymer electrolyte
WO1998004008A1 (en) * 1996-07-22 1998-01-29 Motorola Inc. Electrochemical cell having a polymer electrolyte

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
S. K. ZECEVIC ET AL: "Kinetics of O2 Reduction on a Pt Electrode Covered with a Thin Film of Solid Polymer Electrolyte", JOURNAL OF THE ELECTROCHEMICAL SOCIETY, vol. 144, no. 9, - 9 September 1997 (1997-09-09), MANCHESTER, NEW HAMPSHIRE US, pages 2973 - 2982, XP002077420 *
W.WIECZOREK ET AL: "PROTONIC HYDROGELS FOR APPLICATION IN AMBIENT TEMPERATURE FUEL CELLS", NEW MATER. FUEL CELL SYST. I, PROC. INT. SYMP., 1ST MONTREAL CANADA JULY 9-13 1995, - 1995, XP002077419 *

Cited By (33)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001018894A3 (en) * 1999-09-09 2001-09-07 Danish Power Systems Aps Polymer electrolyte membrane fuel cells
EP1523053A2 (en) * 1999-09-09 2005-04-13 Danish Power Systems APS Polymer electrolyte membrane fuel cells
US6946211B1 (en) 1999-09-09 2005-09-20 Danish Power Systems Aps Polymer electrolyte membrane fuel cells
WO2001018894A2 (en) * 1999-09-09 2001-03-15 Danish Power Systems Aps Polymer electrolyte membrane fuel cells
EP1523053A3 (en) * 1999-09-09 2010-04-28 Danish Power Systems APS Polymer electrolyte membrane fuel cells
KR100905688B1 (en) * 2001-09-12 2009-07-03 바스프 푸엘 셀 게엠베하 Proton-conducting membrane and the use of the same
DE102006062251A1 (en) * 2006-12-22 2008-06-26 Volkswagen Ag Membrane electrode unit for high temperature gas cell, comprises polymer membrane impregnated with electrolytes, and cathodic- and anodic gas diffusion electrodes placed at cathode- and anode lateral membrane surfaces respectively
DE102007002515A1 (en) 2007-01-17 2008-08-14 Volkswagen Ag Polymer electrolyte membrane useful for high temperature-fuel cell for traction systems or the additional power supply of motor vehicles, comprises an organic polymer material impregnated with an electrolyte, and a laminated structure
DE102007018280A1 (en) 2007-04-18 2008-10-23 Volkswagen Ag Polymer electrolyte membrane manufacturing method for fuel cell, involves impregnating polymer membrane with liquid or solved electrolytes, where polymer membrane is supported between carrier foils that lie at both sides of polymer membrane
DE102007020947A1 (en) 2007-05-04 2008-11-13 Volkswagen Ag Gas diffusion electrode for fuel cell, particularly for high temperature fuel cells based on electrolyte impregnated membranes, has gas diffusion layer and porous catalyst layer arranged on gas diffusion layer
DE102007025207A1 (en) 2007-05-30 2008-12-04 Volkswagen Ag Gas diffusion electrode for high temperature gas cells based on electrolyte-impregnated membrane, comprises gas diffusion layer, and porous catalyst layer arranged on diffusion layer and having conductive substrate and catalytic material
DE102007031280A1 (en) 2007-07-05 2009-01-08 Volkswagen Ag Gas diffusion electrode with membrane-electrode-unit for high temperature fuel cells based on membrane for traction system, has gas diffusion layer and catalyst layer is impregnated with another electrolyte and has hydrophobic material
DE102007044246A1 (en) 2007-09-11 2009-03-12 Volkswagen Ag Membrane electrode unit with hydrogenatable material for a fuel cell
US8283081B2 (en) 2007-09-11 2012-10-09 Volkswagen Aktiengesellschaft Membrane electrode assembly with hydrogenatable material for a fuel cell
DE102007061061A1 (en) 2007-12-14 2009-06-18 Volkswagen Ag Fuel cell stack for traction system of motor vehicle, has hydrogen supply line for supplying hydrogen to anodes and dummy cell, and hydrogen discharge line for removing residual hydrogen from anode and dummy cell
DE102008009437A1 (en) 2008-02-14 2009-09-03 Volkswagen Ag Membrane-electrode unit for high temperature-proton exchange membrane-fuel cell, has polymer electrolyte membrane with polymer membrane impregnated with electrolyte
DE102008019874A1 (en) 2008-04-17 2009-10-22 Volkswagen Ag Method for determining content or partial pressure of gas component in gas mixture of fuel cell, involves detecting sound velocity of gas mixture, where content or partial pressure is determined in dependence of sound velocity
DE102008019874B4 (en) * 2008-04-17 2021-02-18 Audi Ag Method for determining a content or partial pressure of a gas component of a fuel cell
DE102008041225A1 (en) 2008-08-13 2010-02-18 Volkswagen Ag Fuel cell for supplying electricity to e.g. drive motor of motor vehicle, has discharging systems arranged in fuel cell stack that is upstream in hydrogen flow direction and connected with supply systems of downstream fuel cell stack
DE102009001137A1 (en) 2008-10-29 2010-05-06 Volkswagen Ag Polymer electrolyte membrane for fuel cells, comprises a polymer component, an electrolyte mixture, and additive components for increasing proton conductivity of the membrane and for influencing its mechanical- and/or surfaces properties
DE102009001141A1 (en) 2008-10-29 2010-05-06 Volkswagen Ag Producing polymer electrolyte membrane, by producing polymer solution of polyazol in solvent mixture, transferring polymer solution in flat structure, and dropping polymer solution that is transferred in flat structure with liquid water
WO2010145828A3 (en) * 2009-06-20 2011-03-10 Basf Se Method for the production of a high-molecular polyazole
WO2010145827A3 (en) * 2009-06-20 2011-03-10 Basf Se Composition containing polyazole
US8722279B2 (en) 2009-06-20 2014-05-13 Basf Se Polyazole-containing composition
US8669296B2 (en) 2009-06-20 2014-03-11 Basf Se Method for the production of a high-molecular polyazol
CN102803347A (en) * 2009-06-20 2012-11-28 巴斯夫欧洲公司 Method For The Production Of A High-molecular Polyazole
DE102009028308A1 (en) 2009-08-06 2011-02-10 Volkswagen Ag Membrane electrode unit, useful in fuel cell, comprises a polymer electrolyte membrane made of a polymer, two electrodes sandwiching polymer electrolyte membrane, an electrolyte wetting polymer electrolyte membrane and silicate derivative
DE102009028758A1 (en) 2009-08-20 2011-02-24 Volkswagen Ag Long-term stable polymer electrolyte membrane for HT fuel cells and process for their preparation
WO2011020872A1 (en) 2009-08-20 2011-02-24 Volkswagen Ag Long-term stable polymer electrolyte membrane for ht fuel cells and method for the production thereof
WO2011069593A1 (en) 2009-12-10 2011-06-16 Volkswagen Aktiengesellschaft Method for producing a catalytic material for electrodes of a fuel cell
DE102009057797A1 (en) 2009-12-10 2011-06-16 Volkswagen Ag Method for producing a catalytic material for electrodes of a fuel cell
CN102386424A (en) * 2010-08-31 2012-03-21 爱信精机株式会社 Fuel cell electrolyte membrane, membrane electrode assembly, fuel cell and method of manufacturing fuel cell electrolyte membrane
EP2424026A1 (en) * 2010-08-31 2012-02-29 Aisin Seiki Kabushiki Kaisha Fuel cell electrolyte membrane, membrane electrode assembly, fuel cell and method of manufacturing fuel cell electrolyte membrane

Also Published As

Publication number Publication date
EP0996990A1 (en) 2000-05-03
ATE251805T1 (en) 2003-10-15
EP0996990B1 (en) 2003-10-08
DE69818826T2 (en) 2004-08-12
US5945233A (en) 1999-08-31
DE69818826D1 (en) 2003-11-13
CN100377410C (en) 2008-03-26
CA2306481C (en) 2007-07-10
DK0996990T3 (en) 2004-01-05
JP2001510931A (en) 2001-08-07
AU7691498A (en) 1999-02-10
CA2306481A1 (en) 1999-01-28
KR100511152B1 (en) 2005-08-31
JP4754687B2 (en) 2011-08-24
BR9811508A (en) 2000-09-26
CN1280710A (en) 2001-01-17
KR20010021896A (en) 2001-03-15
TW432743B (en) 2001-05-01

Similar Documents

Publication Publication Date Title
US5945233A (en) Process for producing polybenzimidazole pastes and gels for use in fuel cells
US6042968A (en) Process for producing polybenzimidazole fabrics for use in fuel
US7682722B2 (en) Membrane-electrode assembly, polymer membranes for a membrane-electrode assembly, polymer electrolyte fuel cells, and methods for the production thereof
JPH11503262A (en) Proton conductive polymer
EP1901378A1 (en) Proton conducting polymer membrane, method for producing same, and fuel cell using same
JP4435746B2 (en) Fuel cell electrolyte, membrane electrode assembly, and method for producing fuel cell electrolyte
CN101999188B (en) Proton conductive polymer electrolyte membrane, process for producing the proton conductive polymer electrolyte membrane, and membrane-electrode assembly and polymer electrolyte fuel cell using the proton conductive polymer electrolyte membrane
JP4435747B2 (en) Fuel cell electrolyte, membrane electrode assembly, and method for producing fuel cell electrolyte
CN102017256B (en) Electrolyte film for a solid polymer type fuel cell and method for producing same
JP4435745B2 (en) Fuel cell electrolyte, membrane electrode assembly, and method for producing fuel cell electrolyte
KR100884959B1 (en) Preparation of Membrane Electrode AssemblyMEA for Polymer Electrolyte Fuel Cell Using Hydrocarbon Based Polymers
AU2002356654B2 (en) Fuel cell and membrane-electrode assembly thereof
KR101138871B1 (en) Polymer electrolyte membrane, manufacturing method thereof, and fuel cell employing the same
CN117352796A (en) Proton exchange membrane and preparation method thereof
JP2005209379A (en) Gel electrolyte, electrode for fuel cell, and fuel cell
Zaidi et al. Solid polymer composite electrolytes for PEMFC
PL180683B1 (en) Proton-conductive membrane and method of making same

Legal Events

Date Code Title Description
WWE Wipo information: entry into national phase

Ref document number: 98807281.5

Country of ref document: CN

AK Designated states

Kind code of ref document: A1

Designated state(s): AU BR CA CN JP KR MX

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE

DFPE Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101)
121 Ep: the epo has been informed by wipo that ep was designated in this application
WWE Wipo information: entry into national phase

Ref document number: 1998924836

Country of ref document: EP

ENP Entry into the national phase

Ref document number: 2306481

Country of ref document: CA

Ref document number: 2306481

Country of ref document: CA

Kind code of ref document: A

WWE Wipo information: entry into national phase

Ref document number: 1020007000460

Country of ref document: KR

WWP Wipo information: published in national office

Ref document number: 1998924836

Country of ref document: EP

WWP Wipo information: published in national office

Ref document number: 1020007000460

Country of ref document: KR

WWG Wipo information: grant in national office

Ref document number: 1998924836

Country of ref document: EP

WWG Wipo information: grant in national office

Ref document number: 1020007000460

Country of ref document: KR