EP1678778A2

EP1678778A2 - Proton-conducting polymer membrane containing polymers with sulfonic acid groups that are covalently bonded to aromatic groups, membrane electrode unit, and use thereof in fuel cells

Info

Publication number: EP1678778A2
Application number: EP04764851A
Authority: EP
Inventors: Joachim Kiefer; Oemer Uensal
Original assignee: Pemeas GmbH
Current assignee: BASF Fuel Cell Research GmbH
Priority date: 2003-09-04
Filing date: 2004-09-04
Publication date: 2006-07-12
Also published as: WO2005024988A2; US20070055045A1; WO2005024988A3; JP2007504616A; DE10340927A1

Abstract

Disclosed is a proton-conducting polymer membrane containing polymers with sulfonic acid groups that are covalently bonded to aromatic groups and polymers which comprise phosphonic acid groups and are obtained by polymerizing monomers encompassing phosphonic acid groups.

Description

description

Proton-conducting polymer membrane containing polymers with sulfonic acid groups covalently bonded to aromatic groups, membrane-electrode unit and their use in fuel cells

The present invention relates to a proton-conducting polymer membrane containing polymers with sulfonic acid groups covalently bonded to aromatic groups, which can be used in a variety of ways due to its excellent chemical and thermal properties and is particularly suitable as a polymer electrolyte membrane (PEM) in so-called PEM fuel cells. Furthermore, the present invention relates to membrane-electrode units which comprise the polymer electrolyte membrane.

A fuel cell usually contains an electrolyte and two electrodes separated by the electrolyte. In the case of a fuel cell, one of the two electrodes is supplied with a fuel, such as hydrogen gas or a methanol-water mixture, and the other electrode with an oxidizing agent, such as oxygen gas or air, and chemical energy from the fuel oxidation is thereby converted directly into electrical energy. Protons and electrons are formed in the oxidation reaction.

The electrolyte is for hydrogen ions, i.e. Protons, but not permeable to reactive fuels such as hydrogen gas or methanol and oxygen gas.

A fuel cell generally has several individual cells, so-called MEEs (membrane electrode assemblies), each of which contains an electrolyte and two electrodes separated by the electrolyte.

Solids such as polymer electrolyte membranes or liquids such as phosphoric acid are used as the electrolyte for the fuel cell. Polymer electrolyte membranes have recently attracted attention as electrolytes for fuel cells. In principle, one can differentiate between two categories of polymer membranes.

The first category includes cation exchange membranes consisting of a polymer structure which contains covalently bound acid groups, preferably sulfonic acid groups. The sulfonic acid group changes into an anion with the release of a hydrogen ion and therefore conducts protons. The mobility of the proton and thus the proton conductivity is directly linked to the water content. Due to the very good miscibility of methanol and water, such cation exchange membranes have a high methanol permeability and are therefore unsuitable for applications in a direct methanol fuel cell. If the membrane dries out, for example as a result of high temperature, the conductivity of the membrane and consequently the performance of the fuel cell decrease drastically. The operating temperatures of fuel cells containing such Cation exchange membranes are thus limited to the boiling point of the water. The humidification of the fuels represents a major technical challenge for the use of polymer electrolyte membrane fuel cells (PEMBZ), in which conventional, sulfonated membranes such as Nation are used.

For example, perfluorosulfonic acid polymers are used as materials for polymer electrolyte membranes. The perfluorosulfonic acid polymer (such as Nation) generally has a perfluorocarbon backbone, such as a copolymer of tetrafluoroethylene and trifluorovinyl, and a side chain attached thereto with a sulfonic acid group, such as a side chain with a sulfonic acid group attached to a perfluoroalkylene group.

The cation exchange membranes are preferably organic polymers with covalently bonded acid groups, in particular sulfonic acid. Methods for sulfonating polymers are described in F. Kucera et. al. Polymer Engineering and Science 1988, Vol. 38, No 5, 783-792.

The most important types of cation exchange membranes which have gained commercial importance for use in fuel cells are listed below: The most important representative is the perfluorosulfonic acid polymer Nation ^® (US 3692569). This polymer can be brought into solution as described in US Pat. No. 4,453,991 and then used as an ionomer. Cation exchange membranes are also obtained by filling a porous support material with such an ionomer. Expanded Teflon is preferred as the carrier material (US 5635041).

Another perfluorinated cation exchange membrane can be prepared as described in US5422411 by copolymerization from trifluorostyrene and sulfonyl-modified trifuorostyrene. Composite membranes consisting of a porous carrier material, in particular expanded Teflon, filled with ionomers consisting of such sulfonyl-modified trifluorostyrene copolymers are described in US5834523. US6110616 describes copolymers of butadiene and styrene and their subsequent sulfonation for the production of cation exchange membranes for fuel cells.

Another class of partially fluorinated cation exchange membranes can be made by radiation grafting and subsequent sulfonation. As described in EP667983 or DE19844645, a grafting reaction is preferably carried out on a previously irradiated polymer film with styrene. The sulfonation of the side chains then takes place in a subsequent sulfonation reaction. Crosslinking can also be carried out at the same time as the grafting and the mechanical properties can thus be changed.

In addition to the above membranes, another class of non-fluorinated membranes has been developed by sulfonation of high-temperature stable thermoplastics. That's what membranes are like from sulfonated polyether ketones (DE4219077, EP96 / 01177), sulfonated polysulfone (J. Membr. Sei. 83 (1993) p.211) or sulfonated polyphenylene sulfide (DE19527435) are known, ionomers prepared from sulfonated polyether ketones are described in WO 00/15691.

Furthermore, acid-base blend membranes are known which are produced as described in DE19817374 or WO 01/18894 by mixtures of sulfonated polymers and basic polymers.

To further improve the membrane properties, a cation exchange membrane known from the prior art can be mixed with a high-temperature stable polymer. The production and properties of cation exchange membranes consisting of blends of sulfonated PEK and a) polysulfones (DE4422158), b) aromatic polyamides (42445264) or c) polybenzimidazole (DE19851498) are described.

Sulfonated polybenzimidazoles are also known from the literature.

Thus US-A-4634530) describes sulfonation of an undoped polybenzimidazole film with a sulfonating agent such as sulfuric acid or oleum in the temperature range up to

100 ° C.

Furthermore, Staiti et al (P. Staiti in J. Membr. Sei. 188 (2001) 71) have described the preparation and properties of sulfonated polybenzimidazoles. It was not possible to carry out the sulfonation on the polymer in the solution. When the sulfonating agent is added to the PBI / DMAc solution, the polymer precipitates. For the sulfonation, a PBI film was first produced and this was immersed in a dilute sulfuric acid. For sulfonation, the samples were then treated at temperatures of approx. 475 ° C for 2 minutes. The sulfonated PBI membranes only have a maximum conductivity of 7.5 ^* 10 ^"5 S / cm at a temperature of 160 ° C. The maximum ion exchange capacity is 0.12 meq / g. It has also been shown that such sulfonated PBI membranes are not are suitable for use in a fuel cell.

The production of sulfoalkylated PBI membranes by the reaction of a hydroxyethyl-modified PBI with a sulton is described in US-A-4997892. Based on this technology, sulfopropylated PBI membranes can be produced (Sanui et al in Polym. Adv. Techn. 11 (2000) 544). The proton conductivity of such membranes is 10 ^"3 S / cm and is therefore too low for applications in fuel cells in which 0.1 S / cm are aimed for.

In addition, polymer membranes are known from WO 00/22684, which have a porous material. The water content of the membrane is preferably 20 to 100% by weight, based on the dry weight of the membrane. Accordingly, the proton conductivity is determined by the water content. The disadvantage of all of these cation exchange membranes is the fact that the membrane has to be moistened, the operating temperature is limited to 100 ° C. and the membranes have a high methanol permeability. The cause of these disadvantages is the conductivity mechanism of the membrane, in which the transport of the protons is coupled to the transport of the water molecule. This is called the "vehicle mechanism" (K.-D. Kreuer, Chem. Mater. 1996, 8, 610-641).

As a second category, polymer electrolyte membranes with complexes of basic polymers and strong acids have been developed. For example, WO96 / 13872 and the corresponding US Pat. No. 5,525,436 describe a process for producing a proton-conducting polymer electrolyte membrane, in which a basic polymer, such as polybenzimidazole, is treated with a strong acid, such as phosphoric acid, sulfuric acid, etc.

In J. Electrochem. Soc, Volume 142, No. 7, 1995, p. L121-L123 describes the doping of a polybenzimidazole in phosphoric acid.

In the basic polymer membranes known in the prior art, the mineral acid (usually concentrated phosphoric acid) used to achieve the required proton conductivity is usually added after the shaping of the polyazole film. The polymer serves as a carrier for the electrolyte consisting of the highly concentrated phosphoric acid. The polymer membrane fulfills further essential functions, in particular it must have high mechanical stability and serve as a separator for the two fuels mentioned at the beginning.

Significant advantages of such a membrane doped with phosphoric acid is the fact that a fuel cell in which such a polymer electrolyte membrane is used can be operated at temperatures above 100 ° C. without the fuels otherwise having to be moistened. This is due to the property of phosphoric acid that the protons can be transported without additional water using the so-called Grotthus mechanism (K.-D. Kreuer, Chem. Mater. 1996, 8, 610-641).

The possibility of operating at temperatures above 100 ° C results in further advantages for the fuel cell system. On the one hand, the sensitivity of the Pt catalyst to gas impurities, especially CO, is greatly reduced. CO arises as a by-product in the reforming of the hydrogen-rich gas from carbon-containing compounds, such as natural gas, methanol or gasoline, or as an intermediate in the direct oxidation of methanol. Typically, the CO content of the fuel must be less than 100 ppm at temperatures <100 ° C. At temperatures in the range of 150-200 °, however, 10,000 ppm CO or more can also be tolerated (NJ Bjerrum et. Al. Journal of Applied Electrochemistry, 2001, 31, 773-779). This leads to significant simplifications of the upstream reforming process and thus to cost reductions for the entire fuel cell system. A great advantage of fuel cells is the fact that the energy of the fuel is converted directly into electrical energy and heat during the electrochemical reaction. Water forms as a reaction product on the cathode. Heat is therefore a by-product of the electrochemical reaction. For applications in which only the electricity is used to drive electric motors, such as for automotive applications, or as a versatile replacement for battery systems, the heat must be dissipated to prevent the system from overheating. Additional, energy-consuming devices are then required for cooling, which further reduce the overall electrical efficiency of the fuel cell. For stationary applications such as the central or decentralized generation of electricity and heat, the heat can be used efficiently using existing technologies such as heat exchangers. High temperatures are aimed at to increase efficiency. If the operating temperature is above 100 ° C and the temperature difference between the ambient temperature and the operating temperature is large, it will be possible to cool the fuel cell system more efficiently or to use small cooling surfaces and to dispense with additional devices compared to fuel cells which, due to the membrane humidification, are below 100 ° C must be operated.

In addition to these advantages, such a fuel cell system also has disadvantages. The durability of membranes doped with phosphoric acid is relatively limited. Here, the service life is significantly reduced, in particular by operating the fuel cell below 100 ° C., for example at 80 ° C. In ^'this context, however, it should be noted that during startup and shutdown of the fuel cell, the cell must be operated at these temperatures.

In addition, the performance, for example the conductivity of known membranes, is still to be improved.

Furthermore, the mechanical stability of known high-temperature membranes with high conductivity can still be improved.

Furthermore, the known membranes doped with phosphoric acid cannot be used in the so-called direct methanol fuel cell (DMBZ). Such cells are of particular interest, however, because a methanol-water mixture is used as fuel. If a known membrane based on phosphoric acid is used, the fuel cell will fail after a very short time.

The present invention is therefore based on the object of providing a novel polymer electrolyte membrane which achieves the objects set out above. In particular, a membrane according to the invention should be able to be produced inexpensively and simply. In addition, it was therefore an object of the present invention to provide polymer electrolyte membranes which have high performance, in particular show high conductivity over a wide temperature range. The conductivity should be achieved without additional humidification, especially at high temperatures. The membrane should have a high mechanical stability in relation to its performance.

Furthermore, a polymer electrolyte membrane should be made available that can be used in many different fuel cells. The membrane is said to be particularly suitable for fuel cells that use pure hydrogen and numerous carbon-containing fuels, in particular natural gas, gasoline, methanol and biomass, as energy sources. In particular, the membrane should be able to be used in a hydrogen fuel cell and in a direct methanol fuel cell (DMBZ).

Furthermore, the operating temperature should be able to be extended from <20 ° C to 200 ° C without reducing the service life of the fuel cell very much.

^• Furthermore, a polymer electrolyte membrane should be created which has a high mechanical stability, for example a high modulus of elasticity, a high tensile strength and a high fracture toughness.

These tasks are solved by a proton-conducting polymer membrane with all the features of claim 1.

The present invention relates to a proton-conducting polymer membrane containing polymers with sulfonic acid groups covalently bonded to aromatic groups and polymers comprising phosphonic acid groups obtainable by polymerizing monomers comprising phosphonic acid groups

According to a particular embodiment of the present invention, preferred proton-conducting polymer membranes can be obtained by a process comprising the steps

A) Preparation of a mixture comprising monomers comprising phosphonic acid groups and at least one polymer with aromatic sulfonic acid groups,

B) applying a layer using the mixture according to step A) on a support,

C) Polymerization of the monomers comprising phosphonic acid groups present in the sheet-like structure obtainable according to step B).

According to a particular aspect of the present invention, preferred proton-conducting polymer membranes are obtainable by a process comprising the steps I) swelling of a polymer film, the polymer film comprising polymer with aromatic sulfonic acid groups, with a liquid containing monomers comprising phosphonic acid groups, and

II) Polymerization of at least some of the monomers comprising phosphonic acid groups, which were introduced into the polymer film in step I).

Swelling means an increase in weight of the film of at least 3% by weight. The swelling is preferably at least 5%, particularly preferably at least 10%.

Determination of the swelling Q is determined gravimetrically from the mass of the film before swelling m ₀ and the mass of the film after the polymerization according to step B), m ₂ . Q = (m ₂ -m ₀ ) / m ₀ x 100

The swelling is preferably carried out at a temperature above 0 ° C., in particular between room temperature (20 ° C.) and 180 ° C. in a liquid which preferably contains monomers comprising at least 5% by weight of phosphonic acid groups. Furthermore, the swelling can also be carried out at elevated pressure. The limits result from economic considerations and technical possibilities.

The polymer film used for swelling generally has a thickness in the range from 5 to 3000 μm, preferably 10 to 1500 μm and particularly preferably. The production of such films from polymers is generally known, some of which are commercially available. The term polymer film means that the film to be used for swelling comprises polymers with aromatic sulfonic acid groups, wherein this film can contain further generally customary additives.

The liquid containing monomers comprising phosphonic acid groups can be a solution, wherein the liquid can also contain suspended and / or dispersed constituents. The viscosity of the liquid which contains monomers comprising phosphonic acid groups can be in a wide range, solvents being added or the temperature being increased in order to adjust the viscosity. The dynamic viscosity is preferably in the range from 0.1 to 10000 mPa * s, in particular 0.2 to 2000 mPa * s, these values being able to be measured, for example, in accordance with DIN 53015.

A membrane according to the invention exhibits a high temperature over a wide temperature range

Conductivity that is also achieved without additional humidification. Here, a membrane according to the invention shows a relatively high mechanical stability.

Furthermore, a membrane according to the invention can be produced simply and inexpensively. Furthermore, these membranes have a surprisingly long service life. Furthermore, a fuel cell that is equipped with a membrane according to the invention can also be operated at low temperatures, for example at 20 ° C., without the service life of the fuel cell being greatly reduced thereby.

A membrane according to the invention exhibits a high conductivity over a wide temperature range, which is also achieved without additional moistening. Furthermore, a fuel cell that is equipped with a membrane according to the invention can also be operated at low temperatures, for example at 80 ° C., without the service life of the fuel cell being greatly reduced thereby.

A polymer electrolyte membrane according to the invention has a very low methanol permeability and is particularly suitable for use in a DMBZ. This enables permanent operation of a fuel cell with a variety of fuels such as hydrogen, natural gas, gasoline, methanol or biomass.

In addition, membranes of the present invention show high mechanical stability, in particular high modulus of elasticity, high tensile strength and high fracture toughness. Furthermore, these membranes have a surprisingly long service life.

Monomers comprising phosphonic acid groups are known in the art. These are compounds which have at least one carbon-carbon double bond and at least one phosphonic acid group. The two carbon atoms which form the carbon-carbon double bond preferably have at least two, preferably 3, bonds to groups which lead to a slight steric hindrance of the double bond. These groups include hydrogen atoms and halogen atoms, especially fluorine atoms. In the context of the present invention, the polymer comprising phosphonic acid groups results from the polymerization product which is obtained by polymerizing the monomer comprising phosphonic acid groups alone or with further monomers and / or crosslinking agents.

The monomer comprising phosphonic acid groups can comprise one, two, three or more carbon-carbon double bonds. Furthermore, the monomer comprising phosphonic acid groups may contain one, two, three or more phosphonic acid groups.

In general, the monomer comprising phosphonic acid groups contains 2 to 20, preferably 2 to 10, carbon atoms. The monomer comprising phosphonic acid groups used to prepare the polymers comprising phosphonic acid groups is preferably a compound of the formula

^ r ^ -R— (P0 ₃ Z ₂ ) _x

wherein

R denotes a bond, a divalent C1-C15 alkylene group, divalent C1-C15 alkyleneoxy group, for example ethyleneoxy group or divalent C5-C20 aryl or heteroaryl group, the above radicals in turn being halogen, -OH, COOZ, -CN, NZ ₂ can be substituted,

Z independently of one another is hydrogen, C1-C15-al yl group, C1-C15-alkoxy group, ethyleneoxy group or C5-C20-aryl or heteroaryl group, it being possible for the above radicals in turn to be substituted with halogen, -OH, -CN, and x is a whole Number 1, 2, 3, 4, 5, 6, 7, 8, 9 or 10 means y an integer 1, 2, 3, 4, 5, 6, 7, 8, 9 or 10 and / or of the formula _x (Z ₂ 0 ₃ P) -R- "R— (P0 ₃ Z ₂ ) _x where

R is a bond, a divalent C1 -C15 alkylene group, divalent C1 -C15 alkyleneoxy group, for example ethyleneoxy group or divalent C5-C20-aryl-. or heteroaryl group, where the above radicals can in turn be substituted with halogen, -OH, COOZ, -CN, NZ ₂ , Z independently of one another hydrogen, C1-C15-alkyl group, C1-C15-alkoxy group, ethyleneoxy group or C5-C20-aryl or heteroaryl group, where the above radicals can in turn be substituted with halogen, -OH, -CN, and x denotes an integer 1, 2, 3, 4, 5, 6, 7, 8, 9 or 10 and / or the Formula R- (P0 ₃ Z ₂ ) _x = KA where

A represents a group of the formulas COOR ² , CN, CONR ² ₂ , OR ² and / or R ² , wherein R ^{2 is} hydrogen, a C1-C15-alkyl group, C1-C15-alkoxy group, ethyleneoxy group or C5-C20-aryl or heteroaryl group means, where the above radicals may in turn be substituted with halogen, -OH, COOZ, -CN, NZ ₂ R is a bond, a divalent C1-C15-alkylene group, divalent C1-C15-alkyleneoxy group, for example ethyleneoxy group or divalent C5-C20- aryl or heteroaryl group, where the above radicals can in turn be substituted with halogen, -OH, COOZ, -CN, NZ ₂ , Z independently of one another hydrogen, C1-C15-alkyl group, C1-C15-alkoxy group, ethyleneoxy group or C5-C20-aryl or heteroaryl group, where the above radicals can in turn be substituted by halogen, -OH, -CN, and x denotes an integer 1, 2, 3, 4, 5, 6, 7, 8, 9 or 10.

The preferred monomers comprising phosphonic acid groups include alkenes which have phosphonic acid groups, such as ethenephosphonic acid, propenephosphonic acid, butenephosphonic acid; Acrylic acid and / or methacrylic acid compounds which have phosphonic acid groups, such as, for example, 2-phosphonomethyl-acrylic acid, 2-phosphonomethyl-methacrylic acid, 2-phosphonomethyl-acrylic acid amide and 2-phosphonomethyl-methacrylic acid amide.

Commercial vinylphosphonic acid (ethenephosphonic acid), as is available, for example, from Aldrich or Clahant GmbH, is particularly preferably used. A preferred vinylphosphonic acid has a purity of more than 70%, in particular 90% and particularly preferably more than 97% purity.

The monomers comprising phosphonic acid groups can also be used in the form of derivatives which can subsequently be converted into the acid, the conversion to the acid also being able to take place in the polymerized state. These derivatives include in particular the salts, the esters, the amides and the halides of the monomers comprising phosphonic acid groups.

The mixture produced in step A) or the liquid used in step I) preferably comprises at least 20% by weight, in particular at least 30% by weight and particularly preferably at least 50% by weight, based on the total weight of the mixture, comprising phosphonic acid groups monomers.

The mixture produced in step A) or the liquid used in step I) can additionally contain further organic and / or inorganic solvents. The organic solvents include in particular polar aprotic solvents such as dimethyl sulfoxide (DMSO), esters such as ethyl acetate and polar protic solvents such as alcohols such as ethanol, propanol, isopropanol and / or butanol. The inorganic solvents include in particular water, phosphoric acid and polyphosphoric acid.

These can have a positive impact on processability. In particular, the solubility of polymers which are formed, for example, in step B) can be improved by adding the organic solvent. The content of monomers comprising phosphonic acid groups in such solutions is generally at least 5% by weight, preferably at least 10% by weight, particularly preferably between 10 and 97% by weight.

According to a particular aspect of the present invention, compositions containing monomers comprising sulfonic acid groups can be used to prepare the polymers comprising phosphonic acid groups.

Monomers comprising sulfonic acid groups are known in the art. These are compounds which have at least one carbon-carbon double bond and at least one sulfonic acid group. The two carbon atoms which form the carbon-carbon double bond preferably have at least two, preferably 3, bonds to groups which lead to a slight steric hindrance of the double bond. These groups include hydrogen atoms and halogen atoms, especially fluorine atoms. In the context of the present invention, the polymer comprising sulfonic acid groups results from the polymerization product which is obtained by polymerization of the monomer comprising sulfonic acid groups alone or with further monomers and / or crosslinking agents.

The monomer comprising sulfonic acid groups can comprise one, two, three or more carbon-carbon double bonds. Furthermore, the monomer comprising sulfonic acid groups may contain one, two, three or more sulfonic acid groups.

In general, the monomer comprising sulfonic acid groups contains 2 to 20, preferably 2 to 10, carbon atoms.

The monomer comprising sulfonic acid groups is preferably a compound of the formula wherein

Z independently of one another denotes hydrogen, C1-C15-alkyl group, C1-C15-alkoxy group, ethyleneoxy group or C5-C20-aryl or heteroaryl group, it being possible for the above radicals themselves to be substituted by halogen, -OH, -CN, and x is an integer 1, 2, 3, 4, 5, 6, 7, 8, 9 or 10 means y an integer 1, 2, 3, 4, 5, 6, 7, 8, 9 or 10

and / or the formula wherein

Z independently of one another denotes hydrogen, C1-C15-alkyl group, C1-C15-alkoxy group, ethyleneoxy group or C5-C20-aryl or heteroaryl group, it being possible for the above radicals themselves to be substituted by halogen, -OH, -CN, and x is an integer 1, 2, 3, 4, 5, 6, 7, 8, 9 or 10 means

and / or the formula R- (S0 ₃ Z) _x

A wherein

A represents a group of the formulas COOR ² , CN, CONR ² ₂ , OR ² and / or R ² , wherein R ^{2 is} hydrogen, a C1-C15-alkyl group, C1-C15-alkoxy group, ethyleneoxy group or C5-C20-aryl or heteroaryl group means, where the above radicals in turn can be substituted with halogen, -OH, COOZ, -CN, NZ ₂ R is a bond, a divalent C1-C15-alkylene group, divalent C1-C15-alkyleneoxy group, for example ethyleneoxy group or divalent C5-C20- Aryl or heteroaryl group, where the above radicals can in turn be substituted with halogen, -OH, COOZ, -CN, NZ ₂ , Z independently of one another hydrogen, C1-C15-alkyl group, C1-C15-alkoxy group, ethyleneoxy group or C5-C20 -Aryl or heteroaryl group, where the above radicals may in turn be substituted with halogen, -OH, -CN, and x denotes an integer 1, 2, 3, 4, 5, 6, 7, 8, 9 or 10.

The preferred monomers comprising sulfonic acid groups include alkenes which have sulfonic acid groups, such as ethene sulfonic acid, propene sulfonic acid, butene sulfonic acid; Acrylic acid and / or methacrylic acid compounds that have sulfonic acid groups, such as 2-sulfonomethyl-acrylic acid, 2-sulfonomethyl-methacrylic acid, 2-sulfonomethyl-acrylic acid amide and 2-sulfonomethyl-methacrylic acid amide.

Commercial vinyl sulfonic acid (ethene sulfonic acid), as is available, for example, from Aldrich or Clariant GmbH, is particularly preferably used. A preferred vinyl sulfonic acid has a purity of more than 70%, in particular 90% and particularly preferably more than 97% purity.

The monomers comprising sulfonic acid groups can also be used in the form of derivatives which can subsequently be converted into the acid, the conversion to the acid also being able to take place in the polymerized state. These derivatives include in particular the salts, the esters, the amides and the halides of the monomers comprising sulfonic acid groups.

According to a particular aspect of the present invention, the weight ratio of monomers comprising sulfonic acid groups to monomers comprising phosphonic acid groups can be in the range from 100: 1 to 1: 100, preferably 10: 1 to 1:10 and particularly preferably 2: 1 to 1: 2.

In a further embodiment of the invention, monomers capable of crosslinking can be used in the production of the polymer membrane. These monomers can be added to the composition according to step A). In addition, the monomers capable of crosslinking can also be applied to the flat structure according to step B). Furthermore, these monomers can be added to the liquid in accordance with step l).

The monomers capable of crosslinking are, in particular, compounds which have at least 2 carbon-carbon double bonds. Dienes, trienes, tetraenes, dimethylacrylates, trimethylacrylates, tetramethylacrylates, diacrylates, triacrylates, tetraacrylates are preferred.

Dienes, trienes and tetraenes of the formula are particularly preferred

Dimethylacrylates, Trimethylycrylate, Tetramethylacrylate of the formula

Diacrylates, triacrylates, tetraacrylates of the formula

wherein

R is a C1-C15-alkyl group, C5-C20-aryl or heteroaryl group, NR ^' , -S0 ₂ , PR ^' , Si (R ^' ) ₂ , where the above radicals can in turn be substituted, R ^' independently of one another hydrogen, a C1-C15 alkyl group, C1-C15 alkoxy group, C5-C20 aryl or heteroaryl group and n is at least 2.

The substituents of the above radical R are preferably halogen, hydroxyl, carboxy, carboxyl, carboxyl esters, nitriles, amines, silyl, siloxane radicals.

Particularly preferred crosslinkers are allyl methacrylate, ethylene glycol dimethacrylate, diethylene glycol dimethacrylate, triethylene glycol dimethacrylate, tetra- and polyethylene glycol dimethacrylate, 1, 3-butanediol dimethacrylate, glycerol dimethacrylate, diurethane dimethacrylate, trimethylolpropane trimethacrylate, epoxy acrylates, for example Ebacryl, N ^', N-methylenebisacrylamide, carbinol, butadiene, isoprene, chloroprene, divinylbenzene and / or bisphenol A dimethylacrylate. These compounds are commercially available, for example, from Sartomer Company Exton, Pennsylvania under the designations CN-120, CN104 and CN-980.

The use of crosslinking agents is optional, these compounds usually being in the range between 0.05 to 30% by weight, preferably 0.1 to 20% by weight, particularly preferably 1 and 10% by weight, based on the weight of the Monomers comprising phosphonic acid groups can be used.

The composition produced according to step A) or the polymer film used in step I) comprises at least one polymer with aromatic sulfonic acid groups. Aromatic sulfonic acid groups are groups in which the sulfonic acid group (-S0 ₃ H) is covalently bound to an aromatic or heteroaromatic group. The aromatic group may be part of the backbone of the polymer or part of a side group, with polymers having aromatic groups in the main chain being preferred. The sulfonic acid groups can often also be used in the form of the salts. Furthermore, it is also possible to use derivatives, for example esters, in particular methyl or ethyl esters, or halides of the sulfonic acids which are converted into the sulfonic acid during operation of the membrane.

Aromatic or heteroaromatic groups preferred according to the invention are derived from benzene, naphthalene, biphenyl, diphenyl ether, diphenylmethane, diphenyldimethylmethane, bisphenone, diphenylsulfone, thiophene, furan, pyrrole, thiazole, oxazole, imidazole, isothiazole, Isoxazole, pyrazole, 1, 3,4-oxadiazole, 2,5-diphenyl-1, 3,4-oxadiazole, 1, 3,4-thiadiazole, 1, 3,4-triazole, 2,5-diphenyl-1, 3,4-triazole, 1, 2,5-triphenyl-1, 3,4-triazole, 1, 2,4-oxadiazole, 1, 2,4-thiadiazole, 1, 2,4-triazole, 1, 2, 3-thazole, 1, 2,3,4-tetrazole, benzo [b] thiophene, benzo [b] furan, indole, benzo [c] thiophene, benzo [c] furan, isoindole, benzoxazole, benzothiazole, benzimidazole, benzisoxazole, Benzisothiazole, benzopyrazole, benzothiadiazole, benzotriazole, dibenzofuran, dibenzothiophene, carbazole, pyridine, bipyridine, pyrazine, pyrazole, pyrimidine, pyridazine, 1, 3,5-triazine, 1, 2,4-triazine, 1, 2,4,5- Triazine, tetrazine, quinoline, isoquinoline, quinoxaline, quinazoline, cinnoline, 1, 8-naphthyridine, 1, 5-naphthyridine, 1, 6-naphthyridine, 1, 7-naphthyhdin, phthalazine, pyridopyrimidine, purine, pteridine or quinolizine, 4H- Quinolizine, diphenyl ether, anthracene, benzopyrrole, benzooxathiadiazole, benzooxadiazole, benzopyridine, benzopyrazine, benzopyrazidine, benzopyrimidine, benzotriazine, indolizine, pyridopyridine, Im idazopyrimidine, pyrazinopyrimidine, carbazole, aciridine, phenazine, benzoquinoline, phenoxazine, phenothiazine, acridizine, benzopteridine, phenanthroline and phenanthrene, which can optionally also be substituted. Preferred substituents are halogen atoms such as. B. fluorine, amino groups, hydroxy groups or alkyl groups.

The substitution pattern is arbitrary, in the case of phenylene, for example, can be ortho-, meta- and para-phenylene. Particularly preferred groups are derived from benzene and biphenylene, which may also be substituted.

Preferred alkyl groups are short-chain alkyl groups with 1 to 4 carbon atoms, such as. B. methyl, ethyl, n- or i-propyl and t-butyl groups.

Preferred aromatic groups are phenyl or naphthyl groups. The alkyl groups and the aromatic groups can be substituted.

The polymers modified with sulfonic acid groups preferably have a sulfonic acid group content in the range from 0.5 to 3 meq / g, preferably 0.5 to 2 meq / g. This value is determined via the so-called ion exchange capacity (IEC).

To measure the IEC, the sulfonic acid groups are converted into the free acid. For this purpose, the polymer is treated with acid in a known manner, excess acid being removed by washing. The sulfonated polymer is first treated in boiling water for 2 hours. Excess water is then dabbed off and the sample is dried for 15 hours at 160 ° C. in a vacuum drying cabinet at p <1 mbar. Then the dry weight of the membrane is determined. The polymer dried in this way is then dissolved in DMSO at 80 ° C. for 1 hour. The solution is then titrated with 0.1 M NaOH. The ion exchange capacity (IEC) is then calculated from the consumption of the acid up to the equivalent point and the dry weight.

Polymers with sulfonic acid groups covalently bonded to aromatic groups are known in the art. For example, polymers with aromatic sulfonic acid groups can be produced by sulfonation of polymers. Methods for sulfonating polymers are described in F. Kucera et. al. Polymer Engineering and Science 1988, Vol. 38, No 5, 783-792. The sulfonation conditions can be selected so that a low degree of sulfonation is produced (DE-A-19959289).

With regard to polymers with aromatic sulfonic acid groups, the aromatic radicals of which are part of the side group, reference is made in particular to polystyrene derivatives. For example, US-A-6110616 describes copolymers of butadiene and styrene and their subsequent sulfonation for use in fuel cells.

Furthermore, such polymers can also be obtained by polyreactions of monomers which comprise acid groups. Thus, perfluorinated polymers as described in US-A-5422411 can be prepared by copolymerization from trifluorostyrene and sulfonyl-modified trifuorostyrene.

In a particular aspect of the present invention abile thermoplastics are hochtemperaturst ^'used which have sulfonic acid groups attached to aromatic groups. In general, such polymers have aromatic groups in the main chain. Thus, sulfonated polyether ketones (DE-A-4219077, WO96 / 01177), sulfonated polysulfones (J. Membr. Sei. 83 (1993) p.211) or sulfonated polyphenylene sulfide (DE-A-19527435) are preferred.

The polymers set out above with sulfonic acid groups bonded to aromatics can be used individually or as a mixture, with particular preference being given to mixtures which have polymers with aromatics in the main chain.

The molecular weight of the polymers with sulfonic acid groups bonded to aromatics can, depending on the type of polymer and its processability, be in wide ranges. The weight average molecular weight M _w is preferably in the range from 5,000 to 10,000,000, in particular 10,000 to 1,000,000, particularly preferably 15,000 to 50,000. According to a particular aspect of the present invention, polymers having sulfonic acid groups bonded to aromatics and having a low polydispersity index M _w / M _n have. The polydispersity index is preferably in the range 1 to 5, in particular 1 to 4.

For use in fuel cells with a continuous use temperature above 100 ° C, preference is given to those polymers having sulfonic acid groups bonded to aromatic groups which have a glass transition temperature or Vicat softening temperature VST / A / 50 of at least 100 ° C, preferably at least 120 ° C and very particularly preferably at least 150 ° C. According to a particular aspect of the present invention, the weight ratio of polymer with monomers covalently bonded to aromatic groups to monomers comprising phosphonic acid groups is in the range from 0.1 to 50, preferably from 0.2 to 20, particularly preferably from 1 to 10.

A further polymer can be added to the composition produced in step A) or the liquid used in step I) which does not comprise any sulfonic acid groups bound to aromatics. This polymer can be dissolved, dispersed or suspended, among other things.

The preferred polymers include polyolefins such as poly (chloroprene),

Polyacetylene, polyphenylene, poly (p-xylylene), polyarylmethylene, polystyrene, polymethylstyrene,

Polyvinyl alcohol, polyvinyl acetate, polyvinyl ether, polyvinylamine, poly (N-vinylacetamide),

Polyvinylimidazole, polyvinyl carbazole, polyvinyl pyrrolidone, polyvinyl pyridine, polyvinyl chloride,

Polyvinylidene chloride, polytetrafluoroethylene, polyvinyl difluoride, polyhexafluoropropylene,

Polyethylene tetrafluoroethylene, copolymers of PTFE with hexafluoropropylene, with

Perfluoropropyl vinyl ether, with trifluoronitrosomethane, with carbalkoxy-perfluoroalkoxy vinyl ether,

Polychlorotrifluoroethylene, polyvinyl fluoride, polyvinylidene fluoride, polyacrolein, polyacrylamide,

Polyacrylonitrile, polycyanoacrylates, polymethacrylimide, cycloolefinic copolymers, in particular from norbomene;

Polymers with C-O bonds in the main chain, for example

Polyacetal, polyoxymethylene, polyether, polypropylene oxide, polyepichlorohydrin,

Polytetrahydrofuran, polyphenylene oxide, polyether ketone, polyether ether ketone,

Polyether ketone ketone, polyether ether ketone ketone, polyether ketone ether ketone ketone

, Polyester, in particular polyhydroxyacetic acid, polyethylene terephthalate,

Polybutylene terephthalate, polyhydroxybenzoate, polyhydroxypropionic acid, polypropionic acid,

Polypivalolactone, polycaprolactone, furan resins, phenol aryl resins, polymalonic acid,

polycarbonate;

Polymeric C-S bonds in the main chain, for example polysulfide ether,

Polyphenylene sulfide, polyether sulfone, polysulfone, polyether ether sulfone, polyaryl ether sulfone,

Polyphenylene sulfone, polyphenylene sulfide sulfone, poly (phenylisulfide-1,4-phenylene;

Polymeric C-N bonds in the main chain, for example

Polyimines, polyisocyanides, polyether brain. ^'' Polyetherimides, poly (trifluoromethyl bis (phthalimide) phenyl, polyaniline, polyaramides, polyamides, polyhydrazides, polyurethanes,

Polyimides, polyazoles, polyazole ether ketone, polyureas, polyazines;

Liquid crystalline polymers, especially Vectra as well

Inorganic polymers, for example polysilanes, polycarbosilanes, polysiloxanes,

Polysilicic acid, polysilicates, silicones, polyphosphazenes and polythiazyl.

These polymers can be used individually or as a mixture of two, three or more polymers. Polymers which contain at least one nitrogen atom, oxygen atom and / or sulfur atom in a repeating unit are particularly preferred. Particularly preferred are polymers which contain at least one aromatic ring with at least one nitrogen, oxygen and / or sulfur heteroatom per repeating unit. Polymers based on polyazoles are particularly preferred within this group. These basic polyazole polymers contain at least one aromatic ring with at least one nitrogen heteroatom per repeat unit.

The aromatic ring is preferably a five- or six-membered ring with one to three nitrogen atoms, which can be fused to another ring, in particular another aromatic ring.

Polymers based on polyazole generally contain recurring azole units of the general formula (I) and / or (II) and / or (III) and / or (IV) and / or (V) and / or (VI) and / or ( VII) and / or (VIII) and / or (IX) and / or (X) and / or (XI) and / or (XII) and / or (XIII) and / or (XIV) and / or (XV) and / or (XVI) and / or (XVI) and / or (XVII) and / or (XVIII) and / or (XIX) and / or (XX) and / or (XXI) and / or (XXII)

NN (V) ^ X ^ ⁿ

--Ar ⁷ - _πr Ar ⁷ -

R

wherein

Ar are the same or different and for a tetra-bonded aromatic or heteroaromatic group, which can be mono- or polynuclear, Ar ^{1 are the} same or different and for a divalent aromatic or heteroaromatic group, which can be mono- or polynuclear, Ar ^{2 are the} same or different Ar ^{3 are the} same or different for a two or three-membered aromatic or heteroaromatic group, which may be mono- or polynuclear, and for a tridentic aromatic or heteroaromatic group, which may be single or polynuclear, Ar ^{4 are the} same or different and for a three-membered aromatic or heteroaromatic group which may be mono- or polynuclear, Ar ^{5 are the} same or different and for a tetra-aromatic or heteroaromatic group which may be mono- or polynuclear, Ar ^{6 are the} same or different and for a divalent aromatic or heteroaromatic group, which can be mononuclear or polynuclear, Ar ⁷ identical or ve are different and for a divalent aromatic or heteroaromatic group, which can be mono- or polynuclear, Ar ^{8 are the} same or different and for a trivalent aromatic or heteroaromatic group, which can be mono- or polynuclear, Ar ^{9 are the} same or different and for a bi- or tri- or tetra-bonded aromatic or heteroaromatic group, which may be mono- or polynuclear, Ar ^{10 are the} same or different and, for a di- or tri-bonded aromatic or heteroaromatic group, which may be mono- or polynuclear, Ar ^{11 is the} same or are different and for a divalent aromatic or heteroaromatic group, which may be mono- or polynuclear, X is the same or different and for oxygen, sulfur or an amino group which has a hydrogen atom, a group having 1-20 carbon atoms, preferably a branched or is not branched alkyl or alkoxy group, or an aryl group as a further radical R is identical or he is different from hydrogen, an alkyl group and an aromatic group is the same or different is hydrogen, an alkyl group and an aromatic group with the proviso that R in formula XX is a divalent group, and n, m is an integer greater than or equal to 10, is preferably greater than or equal to 100.

Aromatic or heteroaromatic groups preferred according to the invention are derived from benzene, naphthalene, biphenyl, diphenyl ether, diphenylmethane, diphenyldimethylmethane, bisphenone, diphenylsulfone, thiophene, furan, pyrrole, thiazole, oxazole, imidazole, isothiazole, isoxazole, 3,4-oxazole, pyrazole , 2,5-diphenyl-1, 3,4-oxadiazoI, 1, 3,4-thiadiazole, 1, 3,4-triazole, 2,5-diphenyI-1, 3,4-triazole, 1, 2.5 -Triphenyl-1, 3,4-triazole, 1, 2,4-oxadiazole, 1, 2,4-thiadiazole, 1, 2,4-triazole, 1, 2,3-triazole, 1, 2,3,4 -Tetrazole, Benzo [b] thiophene, Benzo [b] furan, Indole, benzo [c] thiophene, benzo [c] furan, isoindole, benzoxazole, benzothiazole, benzimidazole, benzisoxazole, benzisothiazole, benzopyrazole, benzothiadiazole, benzotriazole, dibenzofuran, dibenzothiophene, carbazole, pyridine, bipyridine, pyridine, pyridine, pyridine, pyrazine, pyridine, pyridine, pyridine, pyridine, pyridine, pyridine, pyridine, pyridine, pyridine, pyridine, pyridine, pyridine, pyridine, pyridine, pyridine, pyridine, pyridine, pyridine, pyridine, pyridine, pyridine, pyridine, pyridine, pyridine, pyridine, pyridine, pyridine, pyridine, pyridine, pyridine, pyridine, pyrazine 1, 3,5-triazine,, 2,4-triazine, 1, 2,4,5-triazine, tetrazine, quinoline, isoquinoline, quinoxaline, quinazoline, cinnoline, 1, 8-naphthyhdin, 1, 5-naphthyridine, 1 , 6-naphthyridine, 1, 7-naphthyridine, phthalazine, pyridopyrimidine, purine, ptehdin or quinolizine, 4H-quinolizine, diphenyl ether, anthracene, benzopyrrole, benzooxathiadiazole, benzooxadiazole, benzopyridine, benzopyrazine, benzopyimididine, benzopyrazidine, , Pyrazinopyrimidine, carbazole, aciridine, phenazine, benzoquinoline, phenoxazine, phenothiazine, achdizine, benzopteridine, phenanthroline and phenanthrene, which can optionally also be substituted.

The substitution pattern of Ar ¹ , Ar ⁴ , Ar ⁶ , Ar ⁷ , Ar ⁸ , Ar ⁹ , Ar ¹⁰ , Ar ^{11 is} arbitrary, in the case of phenylene, for example, Ar ¹ , Ar ⁴ , Ar ⁶ , Ar ⁷ , Ar ⁸ , Ar ⁹ , Ar ¹⁰ , Ar ^{11 are} ortho-, meta- and para-phenylene. Particularly preferred groups are derived from benzene and biphenylene, which may also be substituted.

Preferred substituents are halogen atoms such as. B. fluorine, amino groups, hydroxyl groups or short-chain alkyl groups such as. B. methyl or ethyl groups.

Preference is given to polyazoles having repeating units of the formula (I) in which the radicals X are the same within a repeating unit.

In principle, the polyazoles can also have different recurring units which differ, for example, in their X radical. However, it preferably has only the same X radicals in a recurring unit.

Other preferred polyazole polymers are polyimidazoles, polybenzthiazoles, polybenzoxazoles, polyoxadiazoles, polyquinoxaiines, polythiadiazoles poly (pyridines), poly (pyrimidines), and poly (tetrazapyrenes).

In a further embodiment of the present invention, the polymer containing recurring azole units is a copolymer or a blend which contains at least two units of the formulas (I) to (XXII) which differ from one another. The polymers can be present as block copolymers (diblock, triblock), statistical copolymers, periodic copolymers and / or alternating polymers. In a particularly preferred embodiment of the present invention, the polymer containing recurring azole units is a polyazole which contains only units of the formula (I) and / or (II).

The number of repeating azole units in the polymer is preferably an integer greater than or equal to 10. Particularly preferred polymers contain at least 00 repeating azole units.

In the context of the present invention, polymers containing recurring benzimidazole units are preferred. Some examples of the extremely useful polymers containing recurring benzimidazole units are represented by the following formulas:

H

where n and m is an integer greater than or equal to 10, preferably greater than or equal to 100.

Further preferred polyazole polymers are polyimidazoles, polybenzimidazole ether ketone, polybenzthiazoles, polybenzoxazoles, polytriazoles, polyoxadiazoles, polythiadiazoles, polypyrazoles, polyquinoxalines, poly (pyridines), poly (pyrimidines), and poly (tetrazapyrenes). Preferred polyazoles are distinguished by a high molecular weight. This applies in particular to the polybenzimidazoles. Measured as intrinsic viscosity, this is preferably at least 0.2 dl / g, preferably 0.7 to 10 dl / g, in particular 0.8 to 5 dl / g.

Celazole from Celanese is particularly preferred. The properties of the polymer film and polymer membrane can be improved by sieving the starting polymer, as described in German patent application No. 10129458.1.

The mixture produced in step A) or the liquid used in step I) can additionally contain further organic and / or inorganic solvents. The organic solvents include in particular polar aprotic solvents such as dimethyl sulfoxide (DMSO), esters such as ethyl acetate and polar protic solvents such as alcohols such as ethanol, propanol, isopropanol and / or butanol. The inorganic solvents include in particular water, phosphoric acid and polyphosphoric acid. These can have a positive impact on processability. For example, the rheology of the solution can be improved; so that it can be extruded or crocheted more easily.

To further improve the application properties, fillers, in particular proton-conducting fillers, and additional acids can also be added to the membrane. Such substances preferably have an intrinsic conductivity at 100 ° C. of at least 10 ^"6 S / cm, in particular 10 ^{" 5} S / cm. The addition can take place, for example, in step A) and / or step B) or step I). Furthermore, these additives, if they are in liquid form, can also be added after the polymerization in step C) or step II).

Non-limiting examples of proton-conducting fillers are

Sulfates such as: CsHS0 ₄ , Fe (S0 ₄ ) ₂ , (NH ₄ ) ₃ H (S0 ₄ ) ₂ , LiHS0 ₄ , NaHS0 ₄ , KHS0 ₄ , RbS0 ₄ , LiN ₂ H ₅ S0 ₄ , NH ₄ HS0 ₄ , phosphates like Zr ₃ (P0 ₄ ) ₄ , Zr (HP0 ₄ ) ₂ , HZr ₂ (P0 ₄ ) ₃ , U0 ₂ P0 ₄ .3H ₂ 0, H ₈ U0 ₂ P0 ₄ , Ce (HP0 ₄ ) ₂ ,. Ti (HP0 ₄ ) ₂ , KH ₂ PQ ₄ , NaH ₂ P0 ₄ , LiH ₂ P0 ₄ , NH ₄ H ₂ P0 ₄ , CsH ₂ P0 ₄ , CaHP0 ₄ , MgHP0 ₄ , HSbP ₂ O _δ , HSb ₃ P ₂ 0ι , H ₅ Sb ₅ P ₂ O ₂₀ , polyacid such as H ₃ PW ₁₂ 0 ₄ or nH ₂ 0 (n = 21-29), H ₃ SiW ₁₂ O ₄₀ .nH ₂ O (n = 21-29), H _x W0 ₃ , HSbW0 ₆ , H ₃ PMo ₁₂ O ₄₀ , H ₂ Sb ₄ 0n, HTaW0 ₆ , HNb0 ₃ , HTiNb0 ₅ , HTiTa0 ₅ , HSbTe0 ₆ , H ₅ Ti ₄ O _g , HSb0 ₃ , H ₂ Mo0 ₄ Selenite and arsenides such as (NH ₄ ) ₃ H (Se0 ₄ ) ₂ , U0 ₂ As0 ₄ , (NH ₄ ) ₃ H (Se0 ₄ ) ₂ , KH ₂ As0 ₄ , Cs ₃ H (Se0 ₄ ) ₂ , Rb ₃ H ( Se0 ₄ ) ₂ , phosphides such as ZrP, TiP, HfP

Oxides such as Al ₂ 0 ₃ , Sb ₂ 0 ₅ , Th0 ₂ , Sn0 ₂ , Zr0 ₂ , Mo0 ₃

Silicates such as zeolites, zeolites (NH ₄ +), layered silicates, framework silicates, H-natrolites, H-mordenites, NH ₄ -analyses, NH ₄ -sodalites, NH ₄ -galates, H-montmorillonites, acids such as HCI0 ₄ , SbF ₅ Fillers such as carbides, in particular SiC, Si ₃ N ₄ , fibers, in particular glass fibers, glass powders and / or polymer fibers, preferably based on polyazoles.

These additives can be present in the proton-conducting polymer membrane in customary amounts, but the positive properties, such as high conductivity, long service life and high mechanical stability of the membrane, should not be adversely affected by the addition of too large amounts of additives, generally including Membrane after the polymerization in step C) or step II) at most 80% by weight, preferably at most 50% by weight and particularly preferably at most 20% by weight of additives.

Furthermore, this membrane can also contain perfluorinated sulfonic acid additives (preferably 0.1-20% by weight, preferably 0.2-15% by weight, very preferably 0.2-10% by weight). These additives improve performance, increase proximity to the cathode to increase oxygen solubility and diffusion, and decrease the absorption of phosphoric acid and phosphate to platinum. (Eiectroiyte additives for phosphoric acid fuel cells. Gang, Xiao; Hjuler, HA; Olsen, O; Berg, RW; Bjerrum, NJ. Chem. Dep. A, Tech. Univ. Denmark, Lyngby, Den. J. Electrochem. Soc . (1993), 140 (4), 896-902 and Perfluorosulfonimide as an additive in phosphoric acid fuel cell. Razaq, M .; Razaq, A .; Yeager, E .; DesMarteau, Darryl D .; Singh, S. Gase Cent. Electrochem. Sei., Gase West. Reserve Univ., Cleveland, OH, USA. J. Electrochem. Soc. (1989), 136 (2), 385-90.) Non-limiting examples of perfluorinated suifonic acid additives are: trifluomethanesulfonic acid, Kaliumtrifluormethansuifonat, sodium trifluoromethanesulfonate, lithium, Ammoniumtrifluormethansulfonat, Kaliumperfluorohexansulfonat, Natriumperfluorohexansulfonat perfluorohexanesulphonate, lithium, ammonium perfluorohexanesulphonate, perfluorohexanesulphonic acid, potassium nonafluorobutanesulphonate, Natriumnonafluorbutansulfonat, Lithiumnonafluorbutansulfonat, Ammoniumnonafluorbutansulfonat, Cäsiumnonafluorbutansulf onate, triethylammonium perfluorohexasulfonate and perflurosulfoimide.

The formation of the flat structure according to step B) takes place by means of measures known per se (casting, spraying, knife coating, extrusion) which are known from the prior art for polymer film production. Suitable carriers are all carriers which are inert under the conditions. These carriers include, in particular, films made from polyethylene terephthalate (PET), polytetrafluoroethylene (PTFE), polyhexafluoropropylene, copolymers of PTFE with hexafluoropropylene, polyimides, polyphenylene sulfides (PPS) and polypropylene (PP).

The thickness of the flat structure according to step B) is preferably between 10 and 4000 μm, preferably between 15 and 3500 μm, in particular between 20 and 3000 μm, particularly preferably between 30 and 1500 μm and very particularly preferably between 50 and 1200 μm.

The polymerization of the monomers comprising phosphonic acid groups in step C) or step II) is preferably carried out by free radicals. The radical formation can take place thermally, photochemically, chemically and / or electrochemically.

For example, a starter solution containing at least one substance capable of forming radicals can be added to the mixture after the mixture has been heated in accordance with step A). Furthermore, a starter solution can be applied to the flat structure obtained after step B). This can be done by means of measures known per se (e.g. spraying, dipping, etc.) which are known from the prior art. If the membrane is made by swelling, a starter solution can be added to the liquid. This can also be applied to the flat structure after swelling.

Suitable radical formers include azo compounds, peroxy compounds, persulfate compounds or azoamidines. Non-limiting examples include dibenzoyl peroxide, dicumyl peroxide, cumene hydroperoxide, diisopropyl peroxydicarbonate, bis (4-t-butylcyclohexyl) peroxydicarbonate, Dikaliumpersulfat, ammonium peroxydisulfate, ^2,2'-azobis (2-methylpropionitrile) (AIBN), 2,2 ^'azobis- (isobuttersäureamidin ) hydrochloride, benzpinakoi, dibenzyl derivatives, methyl ethylene ketone peroxide, 1, 1-azobiscyclohexane carbonitrile, methyl ethyl ketone peroxide, acetylacetone peroxide, dilauryl peroxide, didecanoyiperoxide, tert-butyl per-2-ethylhexanoate, ketone peroxide, methyl isobutyl ketone peroxy peroxy, oxychloride, cyclohexyl peroxyl peroxyl, oxychloride, 2-ethylhexanoate, peroxide, cyclobutyl peroxide, , 5-bis (2-ethylhexanoyl-peroxy) -2,5-dimethylhexane, tert-butyl peroxy-2-ethylhexanoate, tert-butyl peroxy-3,5,5-trimethyl hexanoate, tert-butyl peroxy-isobutyrate, tert-butyl peroxy acetate, Dicumyl peroxide, 1, 1-bis (tert-butylperoxy) cyclohexane, 1, 1-bis (tert-butylperoxy) 3,3,5-trimethylcyclohexane, cumyl hydroperoxide, tert-butyl hydroperoxide, bis (4-tert-bu tylcyclohexyl) peroxydicarbonate, as well as the radical formers available from DuPont under the name ®Vazo, for example ®Vazo V50 and ®Vazo WS.

Furthermore, radical formers can also be used which form radicals when irradiated. The preferred compounds include α, α-diethoxyacetophenone (DEAP, Upjon Corp), n-butylbenzoin ether (®Trigonal-14, AKZO) and 2,2-dimethoxy-2-phenylacetophenone (© Igacure 651) and 1-benzoylcyclohexanol ( © Igacure 184), bis (2,4,6-trimethylbenzoyl) phenylphosphine oxide (®lrgacure 819) and 1- [4- (2-hydroxyethoxy) phenyl] -2-hydroxy-2-phenylpropan-1-one (© Irgacure 2959), each from Ciba Geigy Corp. are commercially available.

Usually between 0.0001 and 5% by weight, in particular 0.01 to 3% by weight (based on the weight of the monomers comprising phosphonic acid groups) is added Free radical generator added. The amount of radical generator can be varied depending on the desired degree of polymerization.

The polymerization can also be carried out by exposure to IR or NIR (IR = InfraRot, ie light with a wavelength of more than 700 nm; NIR = Near IR, ie light with a wavelength in the range from approx. 700 to 2000 nm or an energy in the range of approx. 0.6 to 1.75 eV).

The polymerization can also be carried out by exposure to UV light with a wavelength of less than 400 nm. This polymerization method is known per se and is described, for example, in Hans Joerg Elias, Macromolecular Chemistry, δ.auflage, Volume 1, p.492-511; D.R. Arnold, N.C. Baird, J.R. Bolton, J.C. D. Brand, P.W. M Jacobs, P.de Mayo, W.R. Ware, Photochemistry-An Introduction, Academic Press, New York and M.K. Mishra, Radical Photopolymerization of Vinyl Monomers, J. Macromol. Sci.-Revs. Macromol. Chem. Phys. C22 (1982-1983) 409.

The polymerization can also be achieved by the action of β, γ and / or electron beams. According to a particular embodiment of the present invention, a membrane is irradiated with a radiation dose in the range from 1 to 300 kGy, preferably from 3 to 250 kGy and very particularly preferably from 20 to 200 kGy.

The polymerization of the monomers comprising phosphonic acid groups in step C) or step II) is preferably carried out at temperatures above room temperature (20 ° C.) and below 200 ° C., in particular at temperatures between 40 ° C. and 150 ° C., particularly preferably between 50 ° C. and 120 ° C. The polymerization is preferably carried out under normal pressure, but can also be carried out under the action of pressure. The polymerization leads to a solidification of the flat structure, this solidification being able to be followed by microhardness measurement. The increase in hardness due to the polymerization is preferably at least 20%, based on the hardness of the sheet-like structure obtained in step B).

According to a special embodiment of the present invention, the membranes have high mechanical stability. This size results from the hardness of the membrane, which is determined by means of microhardness measurement according to DIN 50539. For this purpose, the membrane is successively loaded with a Vickers diamond within 20 s up to a force of 3 mN and the depth of penetration is determined. Accordingly, the hardness at room temperature is at least 0.01 N / mm ² , preferably at least 0.1 N / mm ² and very particularly. preferably at least 1 N / mm ² , without this being intended to impose a restriction. The force is then kept constant at 3 mN for 5 s and the creep is calculated from the penetration depth. In preferred membranes, the creep CHU 0.003 / 20/5 under these conditions is less than 20%, preferably less than 10% and very particularly preferably less than 5%. The module determined by means of microhardness measurement YHU is at least 0.5 MPa, in particular at least 5 MPa and very particularly preferably at least 10 MPa, without any intention that this should impose a restriction.

Depending on the desired degree of polymerization, the flat structure which is obtained after the polymerization is a self-supporting membrane. The degree of polymerization is preferably at least 2, in particular at least 5, particularly preferably at least 30 repeat units, in particular at least 50 repeat units, very particularly preferably at least 100 repeat units. This degree of polymerization is determined by the number average molecular weight M _n , which can be determined by GPC methods. Because of the problems of isolating the polymers comprising phosphonic acid groups contained in the membrane without degradation, this value is determined on the basis of a sample which is carried out by polymerizing monomers comprising phosphonic acid groups without addition of polymer. The proportion by weight of monomers comprising phosphonic acid groups and of radical initiators is kept constant in comparison with the ratios of the manufacture of the membrane. The conversion achieved in a comparative polymerization is preferably greater than or equal to 20%, in particular greater than or equal to 40% and particularly preferably greater than or equal to 75%, based on the monomers comprising phosphonic acid groups used.

The polymers comprising phosphonic acid groups contained in the membrane preferably have a broad molecular weight distribution. The polymers comprising phosphonic acid groups can have a polydispersity M _w / M _n in the range from 1 to 20, particularly preferably from 3 to 10.

The water content of the proton-conducting membrane is preferably at most 15% by weight, particularly preferably at most 10% by weight and very particularly preferably at most 5% by weight.

In this context it can be assumed that the conductivity of the membrane can be based on the Grotthus mechanism, which means that the system does not require additional moistening. Accordingly, preferred membranes comprise portions of polymers comprising low molecular weight phosphonic acid groups. Thus, the proportion of polymers comprising phosphonic acid groups with a degree of polymerization in the range from 2 to 20, preferably at least 10% by weight, particularly preferably at least 20% by weight, based on the weight of the polymers comprising phosphonic acid groups.

The polymerization in step C) or step II) can lead to a decrease in the layer thickness. The thickness of the self-supporting membrane is preferably between 15 and 1000 μm, preferably between 20 and 500 μm, in particular between 30 and 250 μm. The membrane obtained in step C) or step II) is preferably self-supporting, ie it can be detached from the support without damage and then, if necessary, processed further directly.

Following the polymerization in step C) or step II), the membrane can be crosslinked thermally, photochemically, chemically and / or electrochemically on the surface. This hardening of the membrane surface additionally improves the properties of the membrane.

According to a particular aspect, the membrane can be heated to a temperature of at least 150 ° C., preferably at least 200 ° C. and particularly preferably at least 250 ° C. The thermal crosslinking is preferably carried out in the presence of oxygen. The oxygen concentration in this process step is usually in the range from 5 to 50% by volume, preferably 10 to 40% by volume, without any intention that this should impose a restriction.

The crosslinking can also be effected by the action of IR or NIR (IR = InfraRot, ie light with a wavelength of more than 700 nm; NIR = Near IR, ie light with a wavelength in the range from approx. 700 to 2000 nm or an energy in the range of approx. 0.6 to 1.75 eV) and / or UV light. Another method is radiation with β, γ and / or electron beams. The radiation dose is preferably between 5 and 250 kGy, in particular 10 to 200 kGy. Irradiation can take place in air or under inert gas. This improves the performance properties of the membrane, in particular its durability.

Depending on the desired degree of crosslinking, the duration of the crosslinking reaction can be in a wide range. In general, this reaction time is in the range from 1 second to 10 hours, preferably 1 minute to 1 hour, without this being intended to impose any restriction.

According to a particular embodiment of the present invention, the membrane comprises at least 3% by weight, preferably at least 5% by weight and particularly preferably at least 7% by weight, of phosphorus (as an element), based on the total weight of the membrane. The proportion of phosphorus can be determined using an elementary analysis. For this purpose, the membrane is dried at 110 ° C. for 3 hours in a vacuum (1 mbar).

The polymers comprising phosphonic acid groups preferably have a phosphonic acid group content of at least 5 meq / g, particularly preferably at least 10 meq / g. This value is determined via the so-called ion exchange capacity (IEC).

To measure the IEC, the phosphonic acid groups are converted into the free acid, the measurement being carried out before polymerization of the monomers comprising phosphonic acid groups he follows. The sample is then titrated with 0.1 M NaOH. The ion exchange capacity (IEC) is then calculated from the consumption of the acid up to the equivalent point and the dry weight.

The polymer membrane according to the invention has improved material properties compared to the previously known doped polymer membranes. In particular, they already show an intrinsic conductivity in comparison with known undoped polymer membranes. This is due in particular to the presence of polymers containing phosphonic acid groups.

The polymer membrane according to the invention has improved material properties compared to the previously known doped polymer membranes. In particular, they perform better than known doped polymer membranes. This is due in particular to an improved proton conductivity. At temperatures of 120 ° C., this is at least 1 mS / cm, preferably at least 2 mS / cm, in particular at least 5 mS / cm, preferably measured without humidification.

Furthermore, the membranes show a high conductivity even at a temperature of 70 ° C. The conductivity depends, among other things, on the sulfonic acid group content of the membrane. The higher this proportion, the better the conductivity at low temperatures. Here, a membrane according to the invention can be moistened at low temperatures. For this purpose, for example, the compound used as an energy source, for example hydrogen, can be provided with a proportion of water. In many cases, however, the water formed by the reaction is sufficient to achieve humidification.

The specific conductivity is measured by means of impedance spectroscopy in a 4-pole arrangement in potentiostatic mode and using platinum electrodes (wire, 0.25 mm diameter). The distance between the current-consuming electrodes is 2 cm. The spectrum obtained is evaluated using a simple model consisting of a parallel arrangement of an ^ohmic resistance and a capacitor. The sample cross-section of the phosphoric acid-doped membrane is measured immediately before the sample assembly. To measure the temperature dependency, the measuring cell is brought to the desired temperature in an oven and controlled via a Pt-100 thermocouple positioned in the immediate vicinity of the sample. After reaching the temperature, the sample is kept at this temperature for 10 minutes before starting the measurement.

The passage current density when operating with 0.5 M methanol solution and 90 ° C. in a so-called liquid direct methanol fuel cell is preferably less than 100 mA / cm ² , in particular less than 70 mA / cm ^2, particularly preferably less than 50 mA / cm ² and very particularly preferably less than 10 mA / cm ² . The passage current density when operating with a 2 M methanol solution and 160 ° C in a so-called gaseous Direct methanol fuel cell preferably less than 100 mA / cm ² , in particular less than 50 mA / cm ^2, very particularly preferably less than 10 mA / cm ² .

To determine the cross-over current density, the amount of carbon dioxide released at the cathode is measured by means of a CO ₂ sensor. From the value of the C0 ₂ amount thus obtained, as from P. Zelenay, SC Thomas, S. Gottesfeld in S. Gottesfeld, TF filler "Proton Conducting Membrane Fuel Cells II" ECS Proc. Vol. 98-27 p. 300 -308, the passage current density is calculated.

Possible areas of application of the intrinsically conductive polymer membranes according to the invention include use in fuel cells, in electrolysis, in capacitors and in battery systems. Because of their property profile, the polymer membranes can preferably be used in fuel cells, in particular in DMBZ fuel cells (direct methanol fuel cell).

The present invention also relates to a membrane electrode unit which has at least one polymer membrane according to the invention. The membrane electrode assembly has a high performance even with a low content of catalytically active substances, such as platinum, ruthenium or palladium. For this purpose, gas diffusion layers provided with a catalytically active layer can be used.

The gas diffusion layer generally shows electron conductivity. Flat, electrically conductive and acid-resistant structures are usually used for this. These include, for example, carbon fiber papers, graphitized carbon fiber papers, carbon fiber fabrics, graphitized carbon fiber fabrics and / or flat structures which have been made conductive by adding carbon black.

The catalytically active layer contains a catalytically active substance. These include noble metals, in particular platinum, palladium, rhodium, iridium and / or ruthenium. These substances can also be used with one another in the form of alloys. Furthermore, these substances can also be used in alloys with base metals, such as Cr, Zr, Ni, Co and / or Ti. In addition, the oxides of the aforementioned noble metals and / or base metals can also be used.

According to a particular aspect of the present invention, the catalytically active compounds are used in the form of particles which preferably have a size in the range from 1 to 1000 nm, in particular 10 to 200 nm and preferably 20 to 100 nm.

Furthermore, the catalytically active layer can contain conventional additives. These include fluoropolymers such as polytetrafluoroethylene (PTFE) and surface-active substances. According to a particular embodiment of the present invention, the weight ratio of fluoropolymer to catalyst material, comprising at least one noble metal and optionally one or more support materials, is greater than 0.1, this ratio preferably being in the range from 0.2 to 0.6.

According to a particular embodiment of the present invention, the catalyst layer has a thickness in the range from 1 to 1000 μm, in particular from 5 to 500, preferably from 10 to 300 μm. This value represents an average value that can be determined by measuring the layer thickness in the cross section of images that can be obtained with a scanning electron microscope (SEM).

According to a particular embodiment of the present invention, the noble metal content of the catalyst layer is 0.1 to 10.0 mg / cm ² , preferably 0.2 to 6.0 mg / cm ² and particularly preferably 0.3 to 3.0 mg / cm ² , These values can be determined by elemental analysis of a flat sample.

For further information on membrane electrode assemblies, reference is made to the specialist literature, in particular to patent applications WO 01/18894 A2, DE 195 09 748, DE 195 09 749, WO 00/26982, WO 92/15121 and DE 197 57 492. The disclosure contained in the above-mentioned references with regard to the construction and manufacture of membrane electrode assemblies, and the electrodes, gas diffusion layers and catalysts to be selected, is also part of the description.

In a further variant, a catalytically active layer can be applied to the membrane according to the invention and this can be connected to a gas diffusion layer.

In a variant of the present invention, the membrane formation can also take place directly on the electrode instead of on a support. Such a membrane is also the subject of the present invention.

Another object of the present invention is an electrode with a proton-conducting polymer coating containing polymers with sulfonic acid residues which are bonded to aromatic groups, obtainable by a process comprising the steps

B) applying a layer using the mixture from step A) on a ^'electrode,

C) Polymerization of the monomers comprising phosphonic acid groups present in the sheet-like structure obtainable according to step B) For the sake of completeness, it should be noted that all preferred embodiments of a self-supporting membrane also apply accordingly to a membrane applied directly to the electrode.

According to a particular aspect of the present invention, the coating has a thickness between 2 and 3000 μm, preferably between 2 and 2000 μm, in particular between 3 and 1500 μm, particularly preferably 5 to 500 μm and very particularly preferably between 10 to 200 μm, without this there should be a restriction.

The polymerization in step C) leads to a hardening of the coating. The treatment is carried out until the coating has sufficient hardness to be able to be pressed into a membrane electrode assembly. The hardness is sufficient if a membrane treated accordingly is self-supporting. In many cases, however, a lower hardness is sufficient. The hardness determined in accordance with DIN 50539 (microhardness measurement) is generally at least 1 mN / mm ² , preferably at least 5 mN / mm ² and very particularly preferably at least 50 mN / mm ² , without any intention that this should impose a restriction.

An electrode coated in this way can be installed in a membrane-electrode unit, which may have at least one polymer membrane according to the invention.

In a further variant, a catalytically active layer can be applied to the membrane according to the invention and this can be connected to a gas diffusion layer. For this purpose, a membrane is formed in accordance with steps A) to C) and the catalyst is applied. These structures are also the subject of the present invention.

In addition, the membrane according to steps A) to C) can also be formed on a support or a support film which already has the catalyst. After removing the carrier or the carrier film, the catalyst is on the membrane according to the invention. These structures are also the subject of the present invention.

The present invention also relates to a membrane-electrode unit which has at least one coated electrode and / or at least one polymer membrane according to the invention.

Claims

claims

1. Proton-conducting polymer membrane containing polymers with sulfonic acid groups covalently bonded to aromatic groups and polymers comprising phosphonic acid groups obtainable by polymerizing monomers comprising phosphonic acid groups.

2. Proton-conducting polymer membrane according to claim 1, obtainable by a process comprising the steps A) preparation of a mixture comprising monomers comprising phosphonic acid groups and at least one polymer with aromatic sulfonic acid groups, B) applying a layer using the mixture according to step A) on a support, C ) Polymerization of the monomers comprising phosphonic acid groups present in the sheet-like structure obtainable according to step B).

3. The proton-conducting polymer membrane according to claim 1, obtainable by a process comprising the steps I) swelling a polymer film, the polymer film comprising polymer with aromatic sulfonic acid groups, with a liquid which contains monomers comprising phosphonic acid groups, and II) polymerizing at least part of the phosphonic acid groups Monomers that were introduced into the polymer film in step I).

4. Membrane according to one of the preceding claims, characterized in that for the preparation of the polymers comprising phosphonic acid groups, a monomer of the formula comprising phosphonic acid groups

^ - R— (P0 ₃ Z ₂ ) _x where R is a bond, a divalent C1-C15 alkylene group, divalent C1-C15 alkyleneoxy group, for example ethyleneoxy group or divalent C5-C20 aryl or heteroaryl group, the above radicals in turn can be substituted with halogen, -OH, COOZ, -CN, NZ ₂ , Z independently of one another denotes hydrogen, C1-C15-alkyl group, C1-C15-alkoxy group, ethyleneoxy group or C5-C20-aryl or heteroaryl group, the above radicals in turn may be substituted with halogen, -OH, -CN, and x is an integer 1, 2, 3, 4, 5, 6, 7, 8, 9 or 10, y is an integer 1, 2, 3, 4, 5 , 6, 7, 8, 9 or 10 means and / or the formula in which R denotes a bond, a divalent C1-C15 alkylene group, divalent C1-C15 alkyleneoxy group, for example ethyleneoxy group or divalent C5-C20 aryl or heteroaryl group, the above radicals in turn having halogen, -OH, COOZ, -CN, NZ ₂ can be substituted, Z is independently hydrogen, C1-C15-alkyl group, C1-C15-alkoxy group, ethyleneoxy group or C5-C20-aryl or heteroaryl group, the above radicals in turn being substituted by halogen, -OH, -CN can and x is an integer 1, 2, 3, 4, 5, 6, 7, 8, 9 or 10 and / or the formula R- (P0 ₃ Z ₂ ) _x = <A where A is a group of the formulas COOR ² , CN, CONR ² ₂ , OR ² and / or R ² , wherein R ^{2 is} hydrogen, a C1-C15 alkyl group, C1-C15 alkoxy group, ethyleneoxy group or C5-C20 aryl or heteroaryl group, the above radicals in turn can be substituted with halogen, -OH, COOZ, -CN, NZ ₂ R can be a bond, a double-bonded C1-C15-alk ylene group, divalent C1-C15-alkyleneoxy group, for example ethyleneoxy group or divalent C5-C20 aryl or heteroaryl group, where the above radicals can in turn be substituted with halogen, -OH, COOZ, -CN, NZ ₂ , Z independently of one another hydrogen, C1-C15-alkyl group, C1-C15-alkoxy group, ethyleneoxy group or C5-C20-aryl or heteroaryl group, it being possible for the above radicals in turn to be substituted with halogen, -OH, -CN, and x is an integer 1, 2, 3 , 4, 5, 6, 7, 8, 9 or 10 means is used.

Membrane according to one of the preceding claims, characterized in that for the preparation of the polymers comprising phosphonic acid groups, a monomer of the formula comprising sulfonic acid groups wherein R denotes a bond, a divalent C1-C15 alkylene group, divalent C1-C15 alkyleneoxy group, for example ethyleneoxy group or divalent C5-C20 aryl or heteroaryl group, the above radicals in turn having halogen, -OH, COOZ, -CN, NZ ₂ can be substituted,

Z is independently hydrogen, C1-C15-alkyl group, C1-C15-alkoxy group, ethyleneoxy group or C5-C20-aryl or heteroaryl group, where the above radicals can in turn be substituted with halogen, -OH, -CN, and x is an integer 1, 2, 3, 4, 5, 6, 7, 8, 9 or 10 y means an integer 1, 2, 3, 4, 5, 6, 7, 8, 9 or 10 and / or of the formula

wherein

R denotes a bond, a divalent C1-C15 alkylene group, divalent C1-C15 alkyleneoxy group, for example ethyleneoxy group or divalent C5-C20 aryl or heteroaryl group, the above radicals in turn having halogen, -OH, COOZ, -CN, NZ ₂ can be substituted,

Z independently of one another denotes hydrogen, C1-C15-alkyl group, C1-C15-alkoxy group, ethyleneoxy group or C5-C20-aryl or heteroaryl group, where the above radicals can in turn be substituted by halogen, -OH, -CN, and x is an integer 1, 2, 3, 4, 5, 6, 7, 8, 9 or 10 and / or of the formula R- (S0 ₃ Z) _x = \ A wherein

A represents a group of the formulas COOR ² , CN, CONR ² ₂ , OR ² and / or R ² , wherein R ^{2 is} hydrogen, a C1-C15-alkyl group, C1-C15-alkoxy group, ethyleneoxy group or C5-C20-aryl or heteroaryl group means, where the above radicals themselves can be substituted with halogen, -OH, COOZ, -CN, NZ ₂

Z independently of one another denotes hydrogen, C1-C15-alkyl group, C1-C5-alkoxy group, ethyleneoxy group or C5-C20-aryl or heteroaryl group, where the above radicals can in turn be substituted by halogen, -OH, -CN, and x an integer 1, 2, 3, 4,

5, 6, 7, 8, 9 or 10 means is used.

6. Membrane according to one of the preceding claims, characterized in that for the preparation of the polymers comprising phosphonic acid groups, capable monomers are used for crosslinking, which have at least 2 carbon-carbon double bonds.

7. Membrane according to one of the preceding claims 2 to 6, characterized in that the mixture produced in step A) or the liquid used in step I) additionally contains dispersed and / or suspended polymer.

8. Membrane according to one of the preceding claims, characterized in that the polymer with aromatic sulfonic acid groups is selected from sulfonated polyether ketones, sulfonated polysulfones or sulfonated polyphenylene sulfide.

9. Membrane according to one of the preceding claims, characterized in that the content of sulfonic acid groups in the polymer aromatic sulfonic acid groups is in the range from 0.5 to 3 meq / g.

10. Membrane according to one of the preceding claims, characterized in that the molecular weight of the polymer is aromatic sulfonic acid groups in the range from ... to ....

11. Membrane according to one of the preceding claims, characterized in that the polymer membrane is crosslinked by the action of oxygen.

12. Membrane according to one of the preceding claims, characterized in that the polymer membrane has a thickness between 15 and 3000 microns.

13. Electrode with a proton-conducting polymer coating containing polymers with sulfonic acid groups covalently bonded to aromatic groups, obtainable by a process comprising the steps

B) applying a layer using the mixture according to step A) on an electrode,

C) Polymerization of the monomers comprising phosphonic acid groups present in the sheet-like structure obtainable in step B).

14. The electrode of claim 13, wherein the coating has a thickness between 2 and 3000 microns.

15. membrane-electrode assembly containing at least one electrode and at least one membrane according to one or more of claims 1 to 10.

16. membrane electrode assembly containing at least one electrode according to claim 13 or 14 and at least one membrane according to one or more of claims 1 to 12.

17. A fuel cell containing one or more membrane electrode assemblies according to claim 15 or 16.