DE10338404A1 - Composite membrane for fuel cells contains a water-soluble polymer with sulfonic, phosphonic and/or carboxylic groups and zirconium phosphate - Google Patents
Composite membrane for fuel cells contains a water-soluble polymer with sulfonic, phosphonic and/or carboxylic groups and zirconium phosphate Download PDFInfo
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- DE10338404A1 DE10338404A1 DE10338404A DE10338404A DE10338404A1 DE 10338404 A1 DE10338404 A1 DE 10338404A1 DE 10338404 A DE10338404 A DE 10338404A DE 10338404 A DE10338404 A DE 10338404A DE 10338404 A1 DE10338404 A1 DE 10338404A1
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- water
- sulfonic
- phosphonic
- composite membrane
- soluble polymer
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- 239000012528 membrane Substances 0.000 title claims abstract description 25
- 229910000166 zirconium phosphate Inorganic materials 0.000 title claims abstract description 7
- LEHFSLREWWMLPU-UHFFFAOYSA-B zirconium(4+);tetraphosphate Chemical compound [Zr+4].[Zr+4].[Zr+4].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O LEHFSLREWWMLPU-UHFFFAOYSA-B 0.000 title claims abstract description 6
- 239000002131 composite material Substances 0.000 title claims abstract description 5
- 229920003169 water-soluble polymer Polymers 0.000 title claims abstract description 5
- 239000000446 fuel Substances 0.000 title description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 19
- 229920000642 polymer Polymers 0.000 claims abstract description 17
- 238000000034 method Methods 0.000 claims abstract description 10
- 239000002253 acid Substances 0.000 claims abstract description 6
- 238000001704 evaporation Methods 0.000 claims abstract description 4
- 230000008020 evaporation Effects 0.000 claims abstract description 3
- 229910052500 inorganic mineral Inorganic materials 0.000 claims abstract description 3
- 239000011707 mineral Substances 0.000 claims abstract description 3
- 239000000203 mixture Substances 0.000 claims abstract description 3
- 239000010409 thin film Substances 0.000 claims abstract description 3
- 125000000542 sulfonic acid group Chemical group 0.000 claims description 8
- 230000008961 swelling Effects 0.000 claims description 4
- QOKYJGZIKILTCY-UHFFFAOYSA-J hydrogen phosphate;zirconium(4+) Chemical compound [Zr+4].OP([O-])([O-])=O.OP([O-])([O-])=O QOKYJGZIKILTCY-UHFFFAOYSA-J 0.000 claims description 2
- ABLZXFCXXLZCGV-UHFFFAOYSA-N phosphonic acid group Chemical group P(O)(O)=O ABLZXFCXXLZCGV-UHFFFAOYSA-N 0.000 claims description 2
- 125000002843 carboxylic acid group Chemical group 0.000 claims 1
- 239000007789 gas Substances 0.000 claims 1
- 238000010409 ironing Methods 0.000 claims 1
- 238000002360 preparation method Methods 0.000 claims 1
- 150000003457 sulfones Chemical class 0.000 claims 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 13
- 239000010408 film Substances 0.000 description 10
- 239000004696 Poly ether ether ketone Substances 0.000 description 7
- 229920002530 polyetherether ketone Polymers 0.000 description 7
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 6
- 239000000010 aprotic solvent Substances 0.000 description 5
- 229920002492 poly(sulfone) Polymers 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- 239000002904 solvent Substances 0.000 description 5
- 150000001768 cations Chemical class 0.000 description 4
- 125000003277 amino group Chemical group 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 238000005342 ion exchange Methods 0.000 description 3
- 150000003460 sulfonic acids Chemical class 0.000 description 3
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 description 2
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- CMOAHYOGLLEOGO-UHFFFAOYSA-N oxozirconium;dihydrochloride Chemical compound Cl.Cl.[Zr]=O CMOAHYOGLLEOGO-UHFFFAOYSA-N 0.000 description 2
- 229920001169 thermoplastic Polymers 0.000 description 2
- 239000004416 thermosoftening plastic Substances 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 229920000557 Nafion® Polymers 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- VIKNJXKGJWUCNN-XGXHKTLJSA-N norethisterone Chemical compound O=C1CC[C@@H]2[C@H]3CC[C@](C)([C@](CC4)(O)C#C)[C@@H]4[C@@H]3CCC2=C1 VIKNJXKGJWUCNN-XGXHKTLJSA-N 0.000 description 1
- 229920003208 poly(ethylene sulfide) Polymers 0.000 description 1
- 229920006393 polyether sulfone Polymers 0.000 description 1
- 150000003839 salts Chemical group 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 159000000000 sodium salts Chemical class 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- 238000004448 titration Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/06—Organic material
- B01D71/76—Macromolecular material not specifically provided for in a single one of groups B01D71/08 - B01D71/74
- B01D71/82—Macromolecular material not specifically provided for in a single one of groups B01D71/08 - B01D71/74 characterised by the presence of specified groups, e.g. introduced by chemical after-treatment
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0081—After-treatment of organic or inorganic membranes
- B01D67/0093—Chemical modification
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/20—Manufacture of shaped structures of ion-exchange resins
- C08J5/22—Films, membranes or diaphragms
- C08J5/2206—Films, membranes or diaphragms based on organic and/or inorganic macromolecular compounds
- C08J5/2275—Heterogeneous membranes
-
- 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
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2325/00—Details relating to properties of membranes
- B01D2325/26—Electrical properties
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2343/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and containing boron, silicon, phosphorus, selenium, tellurium or a metal; Derivatives of such polymers
- C08J2343/02—Homopolymers or copolymers of monomers containing phosphorus
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2300/00—Electrolytes
- H01M2300/0088—Composites
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2300/00—Electrolytes
- H01M2300/0088—Composites
- H01M2300/0091—Composites in the form of mixtures
-
- 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
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Inorganic Chemistry (AREA)
- Electrochemistry (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Manufacture Of Macromolecular Shaped Articles (AREA)
- Fuel Cell (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
Säure-Base-Blendmembranen sind Stand der Technik. Sie finden Anwendung unter anderem in Membranbrennstoffzellen. Sie bestehen aus einer polymeren Säure und wenigstens einer polymeren Base. Beide Komponenten werden in bekannten Verfahren in aprotischen Lösungmitteln aufgelöst. Das Lösungsmittel wird abgedampft und die Membranen werden gegebenfalls noch einer Nachbehandlung unterzogen.Acid-base blend membranes are state of the art. They are used, inter alia, in membrane fuel cells. They consist of a polymeric acid and at least one polymeric base. Both components are prepared by known methods in aprotic solvents dissolved. The solvent is evaporated and the membranes are optionally one more After treatment.
Nachteil dieses Verfahrens ist die Verwendung der meist hochsiedenden aprotischen Lösungsmitteln. Mit diesen Lösungsmitteln sind die entsprechenden Kosten verbunden. Die Lösungsmittel sind meist gesundheitsschädlich und müssen entsprechend verarbeitet werden. Andererseits gibt es keine Möglichkeit die benötigten Polymere in Lösung zu bringen.disadvantage This method is the use of mostly high boiling aprotic Solvents. With these solvents the corresponding costs are connected. The solvents are mostly harmful to health and have to be processed accordingly. On the other hand, there is no way The necessities Polymers in solution bring to.
Es war nun Aufgabe ein Verfahren zu finden das es ermöglich die aprotischen Lösungsmittel in möglichst geringem Umfang zu verwenden bzw. wenn es geht ganz auf sie zu verzichten.It was now the task to find a method that allows the aprotic solvents in as possible to use a small scale or if it is completely to renounce them.
Beschreibung:Description:
Polymere Sulfonsäuren sind wasserlöslich ab einer Ionenaustauschkapazität (IEC) von ungefähr 1,8 meq/g (Milli äquivalent je Gramm). Die Ionenaustauschkapazität läßt sich über Titrationsmethoden einfach bestimmen. Sulfoniertes PEEK (Polyetheretherketon) ist ab einem IEC von ca. 1,8 in heißem Wasser löslich. Dasselbe gilt für Polysulfone (PSU, PES) und viele weitere sulfonierte oder mit phosphonsäuregruppen versehene Polymere, insbesondere für Thermoplasten.polymers sulfonic acids are water soluble an ion exchange capacity (IEC) of about 1.8 meq / g (milli equivalent per gram). The ion exchange capacity can be easily achieved by titration methods determine. Sulfonated PEEK (polyetheretherketone) is from a IEC of about 1.8 in hot Water soluble. The same applies to Polysulfones (PSU, PES) and many more sulfonated or phosphonic acid groups provided polymers, in particular for thermoplastics.
Die
Erfindung wird nachfolgend exemplarisch auch für PEEK, PSU und PES beschrieben. Das
Verfahren ist jedoch allgemein anwendbar und nicht begrenzt auf
irgendein bestimmtes Polymer. PEEK läßt mit konzentrierter Schwefelsäure problemlos
bis zu einem IEC von 2,7 sulfonieren. Von Kenes et.al. wurden Verfahren
beschrieben zur Herstellung von Polymeren, die basische Gruppen
und Sulfonsäuregruppen
auf demselben Polymerbackbone haben. Also ein PEEK das Sulfonsäuregruppen und
Aminogruppen auf dem gleichen Backbone trägt. Dieses Polymer wurde in
aprotischen Lösungsmitteln aufgelöst und entsprechend
weiter zu einer Membran verarbeitet. Es wurde nun überraschenderweise
gefunden, wenn sich auf dem Polymer Sulfonsäuregruppen mit einem IEC von über 2,0
befinden und gleichzeitig sind auf dem gleichen Polymerbackbone noch
Aminogruppen entsprechend einem IEC von 0,2 bis 0,6 vorhanden, dann
ist das Polymer wasserlöslich,
unter der Voraussetzung, dass die Sulfonsäuregruppen kationenausgetauscht
vorliegen. Die bevorzugten Kationen sind ein- und zweiwertige Kationen,
insbesondere Na+, K+,
Li+, Ca2+, Mg2+, und ZrO2+ (
Dies ermöglicht eine stark vereinfachte Darstellung der Membranen. Sulfoniertes PEEK oder PSU mit einem IEC von 2,2 an Sulfonsäuregruppen und einem IEC von 0,5 an Aminogruppen (S-PEEK-NH2) wird in die Salzform mittels Ionenaustausch überführt. Nach der Darstellungsmethode von Kerres et.al. liegt die Sulfonsäure bereits als Natriumsalz vor. Dieses Polymer, mit den zwei funktionellen Gruppen, wird in Wasser, gegebenenfalls unter Erwärmen, aufgelöst. Danach wird die wässrige Lösung zu einem Film durch Entfernen des Wassers verarbeitet. Beispielsweise geschieht dies durch Gießen der Lösung in eine Petrischale und Abdampfen des Lösungsmittels Wassers in einem Trockenschrank. Durch eine Nachbehandlung der Folie in verdünnter Mineralsäure werden die Sulfonsäuregruppen freigesetzt, die ihrerseits wieder zum Teil eine Säure-Base-Wechselwirkung mit der basischen Komponente eingehen. Durch die sich ausbildenden Wasserstoffbrücken wird die Folie nun wasserunlöslich. Man erhält eine Membran mit sehr guten Protonenleitfähigkeiten.This allows a much simplified representation of the membranes. Sulfonated PEEK or PSU with an IEC of 2.2 at sulfonic acid groups and an IEC of 0.5 at amino groups (S-PEEK-NH 2 ) is converted to the salt form by means of ion exchange. According to the presentation method of Kerres et.al. the sulfonic acid is already present as the sodium salt. This polymer, having the two functional groups, is dissolved in water, optionally with heating. Thereafter, the aqueous solution is processed into a film by removing the water. For example, this is done by pouring the solution in a Petri dish and evaporating the solvent water in a drying oven. By aftertreatment of the film in dilute mineral acid, the sulfonic acid groups are released, which in turn partially undergo an acid-base interaction with the basic component. Due to the forming hydrogen bonds, the film is now water insoluble. This gives a membrane with very good proton conductivities.
Dieses Verfahren läßt sich zusätzlich durdie Verwendung von ZrO2+ ausgetauschten Sulfonsäuren verbessern. Mit Zirkonoxychlorid ausgetauschte polymere Sulfonsäuren (IEC > 2,0) enthaltend eine weitere basische Komponente auf demselben Polymerbackbone werden in Wasser gelöst. Danach auf einer Oberfläche zu einem Film geformt und das Wasser wird durch Verdampfen entfernt. Der Film, potentiell immer noch wasserlöslich, wird mit Phosphorsäure (5–80% Gew.) nachbehandelt. Durch die Nachbehandlung bilden sich die Säuregruppen aus und in der Folge die Wasserstoffbrücken mit der basischen Komponente. Zusätzlich wird in der Membran noch Zirkonphosphat und die entsprechenden Hydrogenphosphate ausgefällt. Man erhält eine Kompositmembran bestehend aus einer polymeren Säure und Base (gleicher Backbone) und einer anorganischen Phase aus Zirkonphosphat und Zirkonhydrogenphosphaten. Durch eine wechselseitige Nachbehandlung der Membran mit Zirkonoxychlorid gelöst in Wasser und/oder einem aprotischen Lösungsmittel und Phosphorsäure wird noch mehr Zirkonphosphat in die Membran eingelagert. Die Quellung der Membran nimmt dadurch sehr stark ab obwohl sie einen hohen IEC an Sulfonsäuregruppen hat. Es sind durch die wechselseitige Nachbehandlung Membranen erhalten worden mit einem spezifischen Widerstand von kleiner als 20 Ohm × cm. Dies ist in der gleichen Größenordnung wie NafionTM von DuPont.This process can be further improved by the use of ZrO 2+ exchanged sulfonic acids. Zirconia chloride-exchanged polymeric sulfonic acids (IEC> 2.0) containing another basic component on the same polymer backbone are dissolved in water. Thereafter, formed on a surface into a film and the water is removed by evaporation. The film, potentially still water-soluble, is post-treated with phosphoric acid (5-80% by weight). After-treatment, the acid groups are formed and subsequently the hydrogen bonds with the basic component. In addition zirconium phosphate and the corresponding hydrogen phosphates are precipitated in the membrane. This gives a composite membrane consisting of a polymeric acid and base (same backbone) and an inorganic phase of zirconium phosphate and zirconium hydrogen phosphates. By a mutual aftertreatment of the membrane with zirconium oxychloride dissolved in water and / or an aprotic solvent and phosphoric acid more zirconium phosphate is incorporated into the membrane. The swelling of the membrane decreases very much even though it has a high IEC at sulfonic acid groups. Membranes have been obtained by the mutual aftertreatment with a specific resistance of less than 20 ohms × cm. This is on the same scale as Nafion ™ by DuPont.
Es wurde nun überraschenderweise eine zweite Verbesserung der Erfindung gefunden. Sulfoniertes PEEK oder PSU mit einem IEC von 1,85 wird in Wasser gelöst zusätzlich wird diese Lösung mit einer wässrigen Lösung von 5–30 Gew.% Zirkonoxychlorid (ZrOCl2) bezogen auf die Trockenmasse des sulfonierten Polymers versetzt. Die Lösung wird zu einem dünnen Film ausgerakelt und das Lösungsmittel wird abgedampft. Dabei wird nicht nur Wasser sondern auch HCl entfernt. Der entstehende Film wird in wässriger Phosphorsäure nachbehandelt. Die Membran wird nun noch ein oder mehrmals in wechselweise in Zirkonoxychloridlösung und wässriger Phosphorsäure nachbehandelt. Nach 2–5 Nachbehandlungsschritten wird die Membran in dest. Wasser von überschüssiger Phosphorsäure befreit. Die Membran hat eine stark verringerte Quellung gegenüber der Vergleichsmembran, die nur aus dem sulfonierten Polymer besteht. Die Membran hat sehr gute Eigenschaften in einer Membranbrennstoffzelle, die mit Wasserstoff betrieben wird. Sie ist ebenso geeignet für Temperaturen über 80°C.It has now surprisingly found a second improvement of the invention. Sulfonated PEEK or PSU with an IEC of 1.85 is dissolved in water in addition to this solution is added with an aqueous solution of 5-30 wt.% Zirkonoxychlorid (ZrOCl 2 ) based on the dry mass of the sulfonated polymer. The solution is doctored to a thin film and the solvent is evaporated. Not only water but also HCl is removed. The resulting film is post-treated in aqueous phosphoric acid. The membrane is then post-treated one or more times in alternating manner in zirconium oxychloride solution and aqueous phosphoric acid. After 2-5 post-treatment steps, the membrane is placed in dist. Water is freed from excess phosphoric acid. The membrane has a greatly reduced swelling compared to the comparison membrane, which consists only of the sulfonated polymer. The membrane has very good properties in a membrane fuel cell, which is operated with hydrogen. It is also suitable for temperatures over 80 ° C.
Nachfolgend eine andere Darstellungweise der Kompositmembran. Sulfoniertes, bevorzugt thermoplastisches, wasserlösliches Polymer wird in Wasser aufgelöst und zu einem dünnen Film ausgerakelt, das Wasser wird abgedampft und man erhält einen Film, bevorzugt ist eine Dicke von 10–100 μm. Danach wird diese Folie in wässrige Zirkonoxychloridlösung für 1 bis 24 Stunden eingelegt. Im nächsten Schritt wird die Folie in verdünnter Phosphorsäure nachbehandelt für ca. 1 bis 24 Stunden. Dieser Vorgang wird 2 bis 5 mal wiederholt. Die Quellung der Membran nimmt mit jedem Nachbehandlungsschritt ab.following another way of displaying the composite membrane. sulfonated preferably thermoplastic, water-soluble polymer is dissolved in water disbanded and to a thin one Film is ripped off, the water is evaporated off and you get a film preferred is a thickness of 10-100 microns. After that This film is in aqueous Zirkonoxychloridlösung for 1 to 24 hours. In the next step The film is diluted in dilute Post-treated phosphoric acid for about. 1 to 24 hours. This process is repeated 2 to 5 times. The Swelling of the membrane decreases with each post-treatment step.
Alternativ zur vorigen Darstellung wird sulfoniertes wasserlösliches Polymer mit Zirkonylkationen, als Kation der Sulfonsäure verwendet. Das Polymer wird in Wasser gelöst und wieder zu einer Membran verarbeitet. Dadurwird ein Nachbehandlungsschritt eingespart.alternative to the previous illustration is sulfonated water-soluble Polymer with zirconyl cations, used as cation of sulfonic acid. The polymer is dissolved in water and processed again into a membrane. This will be an aftertreatment step saved.
Claims (2)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE10338404A DE10338404A1 (en) | 2002-08-15 | 2003-08-18 | Composite membrane for fuel cells contains a water-soluble polymer with sulfonic, phosphonic and/or carboxylic groups and zirconium phosphate |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE10238136 | 2002-08-15 | ||
| DE10238136.4 | 2003-08-15 | ||
| DE10338404A DE10338404A1 (en) | 2002-08-15 | 2003-08-18 | Composite membrane for fuel cells contains a water-soluble polymer with sulfonic, phosphonic and/or carboxylic groups and zirconium phosphate |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| DE10338404A1 true DE10338404A1 (en) | 2005-04-07 |
Family
ID=34258129
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DE10338404A Withdrawn DE10338404A1 (en) | 2002-08-15 | 2003-08-18 | Composite membrane for fuel cells contains a water-soluble polymer with sulfonic, phosphonic and/or carboxylic groups and zirconium phosphate |
Country Status (1)
| Country | Link |
|---|---|
| DE (1) | DE10338404A1 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103566777A (en) * | 2013-11-19 | 2014-02-12 | 天津工业大学 | Preparation of PIM-1 (polymers of intrinsic microporosity-1) gas separation composite membrane provided with ultrathin separation cortex |
| US9023553B2 (en) | 2007-09-04 | 2015-05-05 | Chemsultants International, Inc. | Multilayered composite proton exchange membrane and a process for manufacturing the same |
-
2003
- 2003-08-18 DE DE10338404A patent/DE10338404A1/en not_active Withdrawn
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9023553B2 (en) | 2007-09-04 | 2015-05-05 | Chemsultants International, Inc. | Multilayered composite proton exchange membrane and a process for manufacturing the same |
| CN103566777A (en) * | 2013-11-19 | 2014-02-12 | 天津工业大学 | Preparation of PIM-1 (polymers of intrinsic microporosity-1) gas separation composite membrane provided with ultrathin separation cortex |
| CN103566777B (en) * | 2013-11-19 | 2016-01-20 | 天津工业大学 | A kind of preparation with the corticifugal PIM-1 composite gas separation of ultra-thin parting |
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