DE10133738A1 - Process for producing a plasma-polymerized polymer electrolyte membrane - Google Patents
Process for producing a plasma-polymerized polymer electrolyte membraneInfo
- Publication number
- DE10133738A1 DE10133738A1 DE10133738A DE10133738A DE10133738A1 DE 10133738 A1 DE10133738 A1 DE 10133738A1 DE 10133738 A DE10133738 A DE 10133738A DE 10133738 A DE10133738 A DE 10133738A DE 10133738 A1 DE10133738 A1 DE 10133738A1
- Authority
- DE
- Germany
- Prior art keywords
- plasma
- electrolyte membrane
- producing
- conducting electrolyte
- polymerized ion
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/12—Composite membranes; Ultra-thin membranes
- B01D69/125—In situ manufacturing by polymerisation, polycondensation, cross-linking or chemical reaction
- B01D69/127—In situ manufacturing by polymerisation, polycondensation, cross-linking or chemical reaction using electrical discharge or plasma-polymerisation
-
- 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
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
- H01M8/1018—Polymeric electrolyte materials
- H01M8/102—Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer
- H01M8/1023—Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer having only carbon, e.g. polyarylenes, polystyrenes or polybutadiene-styrenes
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
- H01M8/1018—Polymeric electrolyte materials
- H01M8/102—Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer
- H01M8/1027—Polymeric 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]
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
- H01M8/1018—Polymeric electrolyte materials
- H01M8/102—Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer
- H01M8/103—Polymeric 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]
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
- H01M8/1018—Polymeric electrolyte materials
- H01M8/1039—Polymeric electrolyte materials halogenated, e.g. sulfonated polyvinylidene fluorides
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
- H01M8/1018—Polymeric electrolyte materials
- H01M8/1069—Polymeric electrolyte materials characterised by the manufacturing processes
- H01M8/1072—Polymeric electrolyte materials characterised by the manufacturing processes by chemical reactions, e.g. insitu polymerisation or insitu crosslinking
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
- H01M8/1018—Polymeric electrolyte materials
- H01M8/1069—Polymeric electrolyte materials characterised by the manufacturing processes
- H01M8/1086—After-treatment of the membrane other than by polymerisation
- H01M8/1088—Chemical modification, e.g. sulfonation
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
Abstract
Die Erfindung betrifft ein Verfahren zur Herstellung von Polymer-Elektrolytmembranen mittels plasmaunterstützter Abscheidung aus der Gasphase, welches durch die Wahl seiner Ausgangsstoffe, Kohlenstoff- bzw. Fluor-Kohlenstoff-Verbindungen und Wasser, eine gegenüber dem Stand der Technik deutliche Vereinfachung erzielt.The invention relates to a process for the production of polymer electrolyte membranes by means of plasma-assisted deposition from the gas phase, which, through the choice of its starting materials, carbon or fluorocarbon compounds and water, achieves a significant simplification compared to the prior art.
Description
Die Erfindung betrifft ein Verfahren zur Herstellung von Polymer-Elektrolytmembranen mittels plasmaunterstützter Abscheidung aus der Gasphase, welches durch die Wahl seiner Ausgangsstoffe eine gegenüber dem Stand der Technik deutliche Vereinfachung erzielt. The invention relates to a method for producing polymer electrolyte membranes by means of plasma-assisted deposition from the gas phase, which by the choice of its Starting materials achieved a significant simplification compared to the prior art.
Plasmapolymerisierte Schichten besitzen einen i. a. hohen und zudem einstellbaren Vernetzungsgrad, der zu einer hohen chemischen und thermischen Beständigkeit führt (s. z. B.: R. Hartmann: "Plasmapolymodifizierung von Kunststoffoberflächen", Techn. Rundschau 17 (1988), Seiten 20-23; A. Brunold et al.: "Modifizierung von Polymeren im Niederdruckplasma", Teil 2, mo 51 (1997), Seiten 81-84). Durch die Verwendung von Monomeren, die zum Einbau ionenleitender Gruppen (Sulfonsäure-, Phosphonsäure- oder Carbonsäure- Gruppen) führen, können mit diesem Verfahren ionenleitende Polymermembranen hergestellt werden, welche sich durch ihre Beständigkeit und infolge des hohen Vernetzungsgrades durch ihre Sperrwirkung bezüglich Gas- bzw. Flüssigkeits-Permeation für den Einsatz in Brennstoffzellen, insbesondere Direkt Methanol Brennstoffzellen, oder Elektrolysezellen anbieten. Zudem wird durch die verwendete Abscheidetechnologie die Herstellung dünner Membranen (wenige 10 nm bis einige 10 µm) ermöglicht, welche insbesondere für den Einsatz in miniaturisierten Brennstoffzellensystemen für portable Anwendungen (s. z. B.: DE 196 24 887 A1, DE 199 14 681 A1) oder als Sperrschichten abgeschieden auf herkömmlichen Membranen (DE 199 14 571 A1), wie Phosphorsäure dotierte Polybenzimidazole- Membranen oder Sulfonsäure enthaltende Membranen, von Interesse sind. Plasma polymerized layers have an i. a. high and also adjustable Degree of crosslinking, which leads to a high chemical and thermal resistance (see e.g. R. Hartmann: "Plasma polymodification of plastic surfaces", Techn. Rundschau 17 (1988), pages 20-23; A. Brunold et al .: "Modification of polymers in Niederdruckplasma ", Part 2, mo 51 (1997), pages 81-84). By using monomers that for incorporating ion-conducting groups (sulfonic acid, phosphonic acid or carboxylic acid Groups) can use this method to conduct ion-conducting polymer membranes are produced, which are characterized by their durability and due to the high Degree of crosslinking due to its barrier effect with regard to gas or liquid permeation for use in fuel cells, especially direct methanol fuel cells, or electrolysis cells to offer. In addition, the technology used makes the production thinner Membranes (a few 10 nm to a few 10 µm), which are particularly suitable for Use in miniaturized fuel cell systems for portable applications (see e.g .: DE 196 24 887 A1, DE 199 14 681 A1) or deposited as barrier layers conventional membranes (DE 199 14 571 A1), such as polybenzimidazoles doped with phosphoric acid Membranes or membranes containing sulfonic acid are of interest.
Bereits bekannte plasmapolymerisierte ionenleitende Schichten werden aus verschiedenen Fluorkohlenstoffen in Verbindung mit Trifluormethansulfonsäure (z. B. DE 195 13 292 C1, US 57 50 013 A), Verbindungen mit Carboxylgruppen (DE 196 24 887 A1) oder Vinylphosphonsäure (DE 199 14 681 A1) hergestellt. Bei der Verwendung von Trifluormethansulfonsäure kommt es im Plasma aufgrund der vergleichbaren Bindungsenergien zwischen der Kohlenstoff/Schwefel-Bindung und den Bindungen in der Sulfonsäure auch zur Fragmentierung der Sulfonsäure. Hierdurch entstehen entweder hochvernetzte Polymere mit sehr geringer Ionenleitfähigkeit oder Polymere mit hinreichender Ionenleitfähigkeit aber geringem Vernetzungsgrad und hohem Anteil nicht kovalent an das Polymergerüst gebundener Trifluormethansulfonsäure und damit nicht langzeitstabile Elektrolyte (siehe dazu: Ber. Bunsenges. Phys. Chem., Bd 98 (1994), Seite 631 bis 635). Bei allen erwähnten Säure-Verbindungen ist für die Plasmapolymerisation eine Verdampfung notwendig, welches neben dem nachteiligen Umgang mit gesundheitsgefährdenden Materialien einen erhöhten apparativen Aufwand bedeutet. Already known plasma-polymerized ion-conducting layers are made from different Fluorocarbons in combination with trifluoromethanesulfonic acid (e.g. DE 195 13 292 C1, US 57 50 013 A), compounds with carboxyl groups (DE 196 24 887 A1) or Vinylphosphonic acid (DE 199 14 681 A1) produced. When using Trifluoromethanesulfonic acid occurs in plasma due to the comparable binding energies between the carbon / sulfur bond and the bonds in the sulfonic acid too for the fragmentation of sulfonic acid. This creates either highly networked Polymers with very low ionic conductivity or polymers with sufficient ionic conductivity but low degree of crosslinking and high proportion not covalently to the polymer structure bound trifluoromethanesulfonic acid and thus not long-term stable electrolytes (see on this: Ber. Bunsenges. Phys. Chem., Vol 98 (1994), pages 631 to 635). With all mentioned Acid compounds require evaporation for plasma polymerization, which in addition to the disadvantageous handling of health-endangering materials means increased equipment expenditure.
Eine deutliche Vereinfachung in der Prozessführung und eine deutliche Kostensenkung in der Herstellung bietet die erfindungsgemäße Plasmapolymerisation ionenleitender Schichten mit der Verwendung von Kohlenstoffverbindungen, vorzugsweise Alkene und Alkine, oder Fluorkohlenstoffverbindungen, vorzugsweise fluorierte Alkene, in Kombination mit Wasser. Die Fragmentation des Wassers im Plasma führt zur Bildung von OH-Radikalen, wodurch erst während des Schichtwachstums die für die Ionenleitfähigkeit notwendigen Carboxylgruppen gebildet werden. Durch die Verwendung handelsüblicher Flüssigkeitsmassenflussregler entfällt der bei anderen Säureverbindungen notwendige Verdampfer. Der hohe Dampfdruck des Wassers erlaubt zudem eine Abscheidung bei Raumtemperatur, während bei den erwähnten Säureverbindungen eine Beheizung der Gaszufuhr vom Verdampfer zum Reaktor und der Elektroden notwendig ist, um eine Kondensation der Säureverbindungen in diesen Bereichen zu verhindern. A significant simplification in litigation and a significant cost reduction in The production of the plasma polymerization according to the invention is more ion-conductive Layers with the use of carbon compounds, preferably alkenes and alkynes, or fluorocarbon compounds, preferably fluorinated alkenes, in combination with Water. The fragmentation of water in the plasma leads to the formation of OH radicals, whereby the necessary for the ionic conductivity only during the layer growth Carboxyl groups are formed. By using commercially available The liquid mass flow controller eliminates the evaporator necessary for other acid compounds. The high water vapor pressure also allows separation at room temperature, while with the acid compounds mentioned heating the gas supply from Evaporator to the reactor and the electrodes is necessary to condense the To prevent acid compounds in these areas.
Für die Anwendung dieser neuartigen plasmapolymerisierten Elektrolytmembranen in Brennstoffzellen, insbesondere miniaturisierten Brennstoffzellen, bietet sich für deren Herstellung die Kombination mit in Dünnschichtverfahren (z. B. Kathodenzerstäubung oder Plasmaunterstützte Abscheidung aus der Gasphase) hergestellten Katalysatorschichten und gegebenenfalls porösen leitfähigen Kontaktschichten an (DE 199 14 681 A). Diese Abscheidungen können in einem geeigneten Reaktor, der sowohl Sputterverfahren als auch die Abscheidung aus der Gasphase erlaubt, oder in miteinander verbundenen separaten Reaktoren, in denen jeweils eine Komponente der Membran Elektroden Einheit in Dünnschichtverfahren abgeschieden wird und ein Transport zwischen den Reaktoren im Vakuum erfolgt, durchgeführt werden. Je nach verwendeten Substraten kann dafür ein stationärer Abscheideprozeß der plasmapolymerisierten Elektrolyte, z. B. für die Beschichtung einzelner geeignet strukturierter Glas- oder Siliziumsubstrate, oder ein Durchlaufprozeß, im Falle hoher Stückzahlen oder bei der Abscheidung auf einer geeigneten Folie, vorteilhaft sein. For the application of these new plasma polymerized electrolyte membranes in Fuel cells, in particular miniaturized fuel cells, are suitable for them Manufacture in combination with thin film processes (e.g. sputtering or Plasma-assisted deposition from the gas phase) produced catalyst layers and optionally porous conductive contact layers on (DE 199 14 681 A). This Depositions can be carried out in a suitable reactor that uses both sputtering methods and separation from the gas phase allowed, or in interconnected separate ones Reactors, each in which a component of the membrane electrode unit in Thin film process is deposited and a transport between the reactors in the Vacuum is carried out. Depending on the substrates used, a stationary deposition process of the plasma polymerized electrolytes, e.g. B. for the coating individually suitably structured glass or silicon substrates, or a continuous process, in In case of large quantities or when depositing on a suitable film, advantageous his.
Claims (10)
Priority Applications (8)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE10133738A DE10133738A1 (en) | 2001-07-11 | 2001-07-11 | Process for producing a plasma-polymerized polymer electrolyte membrane |
EP02762348A EP1497882A2 (en) | 2001-07-11 | 2002-07-11 | Method for producing a plasma-polymerized polymer electrolyte membrane and a polyazol membrane coated by plasma-polymerization |
KR10-2003-7016749A KR20040014572A (en) | 2001-07-11 | 2002-07-11 | Method for producing a plasma-polymerized polymer electrolyte membrane and a polyazol membrane coated by plasma-polymerization |
PCT/EP2002/007734 WO2003007411A2 (en) | 2001-07-11 | 2002-07-11 | Method for producing a plasma-polymerized polymer electrolyte membrane and a polyazol membrane coated by plasma-polymerization |
CNA028121287A CN1610984A (en) | 2001-07-11 | 2002-07-11 | Method for producing a plasma-polymerized polymer electrolyte membrane and a polyazol membrane coated by plasma-polymerization |
CA002448447A CA2448447A1 (en) | 2001-07-11 | 2002-07-11 | Method for producing a plasma-polymerized polymer electrolyte membrane and a polyazol membrane coated by plasma-polymerization |
AU2002328339A AU2002328339A1 (en) | 2001-07-11 | 2002-07-11 | Method for producing a plasma-polymerized polymer electrolyte membrane and a polyazol membrane coated by plasma-polymerization |
JP2003513069A JP2005520001A (en) | 2001-07-11 | 2002-07-11 | Method for producing plasma polymerized polymer electrolyte membrane and polyazole membrane coated by plasma polymerization |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE10133738A DE10133738A1 (en) | 2001-07-11 | 2001-07-11 | Process for producing a plasma-polymerized polymer electrolyte membrane |
Publications (1)
Publication Number | Publication Date |
---|---|
DE10133738A1 true DE10133738A1 (en) | 2003-02-06 |
Family
ID=7691424
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE10133738A Withdrawn DE10133738A1 (en) | 2001-07-11 | 2001-07-11 | Process for producing a plasma-polymerized polymer electrolyte membrane |
Country Status (8)
Country | Link |
---|---|
EP (1) | EP1497882A2 (en) |
JP (1) | JP2005520001A (en) |
KR (1) | KR20040014572A (en) |
CN (1) | CN1610984A (en) |
AU (1) | AU2002328339A1 (en) |
CA (1) | CA2448447A1 (en) |
DE (1) | DE10133738A1 (en) |
WO (1) | WO2003007411A2 (en) |
Families Citing this family (22)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE10209419A1 (en) | 2002-03-05 | 2003-09-25 | Celanese Ventures Gmbh | Process for producing a polymer electrolyte membrane and its use in fuel cells |
WO2003074597A1 (en) | 2002-03-06 | 2003-09-12 | Pemeas Gmbh | Proton conducting electrolyte membrane having reduced methanol permeability and the use thereof in fuel cells |
ATE480874T1 (en) | 2002-04-25 | 2010-09-15 | Basf Fuel Cell Gmbh | MULTI-LAYER ELECTROLYTE MEMBRANE |
DE10230477A1 (en) | 2002-07-06 | 2004-01-15 | Celanese Ventures Gmbh | Functionalized polyazoles, processes for their preparation and their use |
CA2494530A1 (en) | 2002-08-02 | 2004-02-19 | Pemeas Gmbh | Proton-conducting polymer membrane comprising a polymer with sulphonic acid groups and use thereof in fuel cells |
DE10239701A1 (en) | 2002-08-29 | 2004-03-11 | Celanese Ventures Gmbh | Production of polymer membrane, used in membrane electrode unit for fuel cell, uses phosphorus and/or sulfur oxy-acid in liquid for hydrolyzing membrane made by heating mixture of polyphosphoric acid and polyazole or precursors |
JP2005537384A (en) * | 2002-08-29 | 2005-12-08 | ペメアス ゲーエムベーハー | Proton conducting polymer membrane manufacturing method, improved polymer membrane and use thereof in fuel cells |
DE10242708A1 (en) * | 2002-09-13 | 2004-05-19 | Celanese Ventures Gmbh | Proton-conducting membranes and their use |
DE10246459A1 (en) | 2002-10-04 | 2004-04-15 | Celanese Ventures Gmbh | Polymer electrolyte membrane for use, e.g. in fuel cells, obtained by heating a mixture of phosphonated aromatic polyazole monomers in polyphosphoric acid and then processing to form a self-supporting membrane |
DE10246372A1 (en) | 2002-10-04 | 2004-04-15 | Celanese Ventures Gmbh | Catalyst-coated polymer electrolyte membrane for use, e.g. in fuel cells, obtained by processing a mixture of polyphosphoric acid and polyazole to form a self-supporting membrane which is then coated with catalyst |
DE10246373A1 (en) | 2002-10-04 | 2004-04-15 | Celanese Ventures Gmbh | Polymer electrolyte membrane for use, e.g. in fuel cells, manufactured by heating a mixture of sulfonated aromatic polyazole monomers in polyphosphoric acid and then processing to form a self-supporting membrane |
US7820314B2 (en) | 2003-07-27 | 2010-10-26 | Basf Fuel Cell Research Gmbh | Proton-conducting membrane and use thereof |
CN100449829C (en) * | 2004-06-30 | 2009-01-07 | Tdk株式会社 | Direct alcohol fuel cell and method for producing same |
KR100727216B1 (en) * | 2004-11-19 | 2007-06-13 | 주식회사 엘지화학 | Novel sulphonated copolymer and electrolyte membrane using the same |
KR100706067B1 (en) * | 2005-01-25 | 2007-04-11 | 한양대학교 산학협력단 | Acid or base-doped porous proton conducting polymer, preparation method thereof, polymer membrane using the same and fuel cell using the same |
DE102006040749A1 (en) * | 2006-08-31 | 2008-03-06 | Daimler Ag | Oxidation-stabilized polymer electrolyte membranes for fuel cells |
FR2908558B1 (en) * | 2006-11-13 | 2008-12-19 | Commissariat Energie Atomique | SILICY ELECTROLYTE MATERIAL FOR FUEL CELL, METHOD FOR PRODUCING THE SAME, AND FUEL CELL USING SUCH MATERIAL. |
FR2928227B1 (en) * | 2008-02-29 | 2010-04-02 | Commissariat Energie Atomique | PROCESS FOR MANUFACTURING ION CONDUCTION POLYMERIC MEMBRANE FOR FUEL CELL. |
WO2012015072A1 (en) * | 2010-07-28 | 2012-02-02 | 住友化学株式会社 | Polymer electrolyte composition, polymer electrolyte and sulfur-containing heterocyclic aromatic compound |
JP2012049118A (en) * | 2010-07-28 | 2012-03-08 | Sumitomo Chemical Co Ltd | Polymer electrolyte, polymer electrolyte film and polyarylene compound |
WO2017217628A1 (en) * | 2016-06-14 | 2017-12-21 | 충남대학교산학협력단 | Method for producing metal nanoparticle-polymer composite thin film |
CN111621208B (en) * | 2020-05-18 | 2021-11-05 | 江苏菲沃泰纳米科技股份有限公司 | Waterproof membrane layer and preparation method, application and product thereof |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3712490A1 (en) * | 1986-04-11 | 1987-10-15 | Applied Membrane Tech | PORE SIZE CONTROL USING PLASMA POLYMERIZATION PROCESS |
DE4234521C1 (en) * | 1992-10-13 | 1994-02-24 | Carbone Ag | Process for producing a composite plasma membrane and its use |
DE19901378A1 (en) * | 1999-01-15 | 2000-07-20 | Fraunhofer Ges Forschung | Process for producing a polymer membrane, in particular a polymer electrolyte membrane for methanol fuel cells, and such a membrane |
DE19914571A1 (en) * | 1999-03-31 | 2001-01-04 | Joerg Mueller | Plasma deposition of polymer to reduce fuel permeability and increase stability of ion-conducting polymer membrane useful in fuel cell uses highly crosslinked polymer of independent composition |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4032440A (en) * | 1975-11-18 | 1977-06-28 | The United States Of America As Represented By The Secretary Of The Interior | Semipermeable membrane |
-
2001
- 2001-07-11 DE DE10133738A patent/DE10133738A1/en not_active Withdrawn
-
2002
- 2002-07-11 KR KR10-2003-7016749A patent/KR20040014572A/en not_active Application Discontinuation
- 2002-07-11 WO PCT/EP2002/007734 patent/WO2003007411A2/en not_active Application Discontinuation
- 2002-07-11 CA CA002448447A patent/CA2448447A1/en not_active Abandoned
- 2002-07-11 CN CNA028121287A patent/CN1610984A/en active Pending
- 2002-07-11 AU AU2002328339A patent/AU2002328339A1/en not_active Abandoned
- 2002-07-11 JP JP2003513069A patent/JP2005520001A/en active Pending
- 2002-07-11 EP EP02762348A patent/EP1497882A2/en not_active Withdrawn
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3712490A1 (en) * | 1986-04-11 | 1987-10-15 | Applied Membrane Tech | PORE SIZE CONTROL USING PLASMA POLYMERIZATION PROCESS |
DE4234521C1 (en) * | 1992-10-13 | 1994-02-24 | Carbone Ag | Process for producing a composite plasma membrane and its use |
DE19901378A1 (en) * | 1999-01-15 | 2000-07-20 | Fraunhofer Ges Forschung | Process for producing a polymer membrane, in particular a polymer electrolyte membrane for methanol fuel cells, and such a membrane |
DE19914571A1 (en) * | 1999-03-31 | 2001-01-04 | Joerg Mueller | Plasma deposition of polymer to reduce fuel permeability and increase stability of ion-conducting polymer membrane useful in fuel cell uses highly crosslinked polymer of independent composition |
Also Published As
Publication number | Publication date |
---|---|
CA2448447A1 (en) | 2003-01-23 |
WO2003007411A2 (en) | 2003-01-23 |
WO2003007411A3 (en) | 2004-11-04 |
JP2005520001A (en) | 2005-07-07 |
AU2002328339A1 (en) | 2003-01-29 |
CN1610984A (en) | 2005-04-27 |
KR20040014572A (en) | 2004-02-14 |
EP1497882A2 (en) | 2005-01-19 |
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