EP1747248A1 - Corps moule anisotrope, procede pour produire et utiliser des corps moules anisotropes - Google Patents

Corps moule anisotrope, procede pour produire et utiliser des corps moules anisotropes

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Publication number
EP1747248A1
EP1747248A1 EP05760686A EP05760686A EP1747248A1 EP 1747248 A1 EP1747248 A1 EP 1747248A1 EP 05760686 A EP05760686 A EP 05760686A EP 05760686 A EP05760686 A EP 05760686A EP 1747248 A1 EP1747248 A1 EP 1747248A1
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European Patent Office
Prior art keywords
group
liquid
acid groups
divalent
monomers
Prior art date
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EP05760686A
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German (de)
English (en)
Inventor
Oemer Uensal
Jörg BELACK
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BASF Fuel Cell Research GmbH
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Pemeas GmbH
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Publication of EP1747248A1 publication Critical patent/EP1747248A1/fr
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    • 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
    • C08J7/00—Chemical treatment or coating of shaped articles made of macromolecular substances
    • C08J7/04—Coating
    • C08J7/06—Coating with compositions not containing macromolecular substances
    • 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
    • C08J7/00—Chemical treatment or coating of shaped articles made of macromolecular substances
    • C08J7/04—Coating
    • C08J7/046—Forming abrasion-resistant coatings; Forming surface-hardening coatings
    • 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
    • C08J5/18—Manufacture of films or sheets
    • 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
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00—Use of organic ingredients
    • C08K5/49—Phosphorus-containing compounds
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L79/00—Compositions of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen with or without oxygen or carbon only, not provided for in groups C08L61/00 - C08L77/00
    • C08L79/04—Polycondensates having nitrogen-containing heterocyclic rings in the main chain; Polyhydrazides; Polyamide acids or similar polyimide precursors
    • 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
    • C08J2379/00—Characterised by the use of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen with or without oxygen, or carbon only, not provided for in groups C08J2361/00 - C08J2377/00
    • C08J2379/04—Polycondensates having nitrogen-containing heterocyclic rings in the main chain; Polyhydrazides; Polyamide acids or similar polyimide precursors
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2203/00—Applications
    • C08L2203/16—Applications used for films

Definitions

  • Anisotropic moldings process for the production and use of anisotropic moldings
  • the present invention relates to anisotropic moldings, processes for producing and using anisotropic moldings, which can be used in particular as proton-conducting electrolyte membranes and as membranes in separation processes.
  • Membranes for technical purposes such as microfiltration, ultrafiltration, reverse osmosis, electrodialysis and pervaporation are generally known and can be obtained commercially. These membranes serve many purposes, but known membranes separate the particles based on chemical properties or their size.
  • membranes are acid-doped polymer membranes, which can be used in a variety of ways due to their excellent chemical, thermal and mechanical properties and are particularly suitable as polymer electrolyte membranes (PEM) in so-called PEM fuel cells.
  • PEM polymer electrolyte membranes
  • the basic polyazole membranes are doped with concentrated phosphoric acid or sulfuric acid and act as proton conductors and separators in so-called polymer electrolyte membrane fuel cells (PEM fuel cells).
  • PEM fuel cells polymer electrolyte membrane fuel cells
  • polymer electrolyte membranes of this type - processed into membrane electrode assemblies (MEE) - can be used in fuel cells at continuous operating temperatures above 100 ° C., in particular above 120 ° C.
  • This high continuous operating temperature allows the activity of the precious metal-based catalysts contained in the membrane electrode assembly (MEE) to be increased.
  • the reformer gas contains significant amounts of carbon monoxide, which usually have to be removed by complex gas processing or gas cleaning.
  • the possibility of increasing the operating temperature means that significantly higher concentrations of CO impurities can be tolerated permanently.
  • the treatment of polyazole films with liquids is described, for example, in German patent application application number 10234236.9.
  • German patent application application number 10209419 describes polymer membranes whose conductivity is based on polymer electrolytes which have a higher durability.
  • the membranes obtained in this way already show a good range of properties. However, improving the entire range of properties is a permanent problem.
  • This range of properties includes, in particular, the methanol permeability, the resting potential and the mechanical properties of the membrane.
  • German patent application application number 10209419 it is disadvantageous in the production method described in German patent application application number 10209419 that the doping takes place in a relatively complex manner, a high manual effort being required in particular. A continuous production of polymer membranes with high durability is not possible or only with great difficulty with the production processes described in the German patent application application number 10209419.
  • the mechanical properties of the film change considerably as a result of the swelling of polymer films with monomers comprising acid groups described in the German patent application application number 10209419.
  • the modulus of elasticity decreases to 5% of the initial value, so that, for example, a polyazole film after doping has only a relatively low mechanical stability.
  • the area of the film increases by up to 80% due to the doping. Because of these problematic properties, these films were doped with acid in a purely manual process by placing the films in an acid bath and then changing the liquid bath several times.
  • the membrane which separates particles, for example proteins, on the basis of their specific shape, for example the length, height and width ratio.
  • the membrane should be mechanically very resilient, thermally stable and chemically resistant, so that this membrane can be used in a variety of ways.
  • the object of the present invention is to provide methods which solve the aforementioned problems.
  • the process was intended to create a simple, safe and reliable process for the production of polymer membranes.
  • the method should have a particularly low liquid consumption.
  • the process should also be inexpensive.
  • the present invention accordingly relates to a process for the production of anisotropic moldings, in which a molded body comprising polymers is passed through a trough filled with liquid, the polymers being unwound from a spool and wound onto a further spool, the liquid comprising monomers comprising phosphonic acid groups and / or monomers comprising sulfonic acid groups.
  • membranes with a relatively constant quality can be achieved by the present method, a particularly low liquid consumption being associated with the method. Furthermore, the method can be carried out inexpensively.
  • an anisotropic shaped body can be obtained by this method.
  • the moldings show an excellent property profile. This range of properties includes, in particular, the methanol permeability, the resting potential and the mechanical properties of a membrane.
  • the membranes according to the invention are mechanically very resilient, thermally stable and chemically resistant. Furthermore, the membranes show excellent separation performance. The membranes separate particles based on a ratio of length, height and width.
  • the solution according to the invention is surprising in particular because the process adapts to the changing properties of the shaped body comprising the polymer, for example that of a film.
  • the film only comes into contact with the liquid in the tub for a very short time, without adversely affecting a treatment.
  • the Treatment of the molded body comprising polymers, for example the film also takes place in the wound state by liquid which is wound up together with the molded body comprising polymers, for example that of a film.
  • Moldings comprising polymers are treated according to the invention. Moldings comprising polymers are known in the technical field.
  • the molded body comprising polymers preferably represents a polymer film.
  • Preferred polymer films have a swelling of at least 3% in the liquid which has monomers comprising phosphonic acid groups and / or monomers comprising sulfonic acid groups.
  • 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 swelling Q is determined gravimetrically from the mass of the film before swelling m 0 and the mass of the film after polymerization of the monomers comprising phosphonic acid groups, m 2 .
  • Q (m 2 -m 0 ) / m 0 x 100
  • the treatment of the polymer films is preferably carried out at a temperature above 0 ° C., in particular between room temperature (20 ° C.) and 180 ° C., with a liquid which preferably contains at least 5% by weight of monomers comprising phosphonic acid groups.
  • the treatment can also be carried out at elevated pressure. The limits result from economic considerations and technical possibilities.
  • the polymer film used for the treatment generally has a thickness in the range from 5 to 3000 ⁇ m, preferably 10 to 1500 ⁇ m 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 the treatment comprises polymers, which film can contain further generally customary additives.
  • polystyrene 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,
  • 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, polyvin
  • Trifluoronitrosomethane with carbalkoxy-perfluoroalkoxy vinyl ether
  • Polychlorotrifluoroethylene polyvinyl fluoride, polyvinylidene fluoride, polyacrolein,
  • Copolymers in particular of norbornene
  • Polyacetal polyoxymethylene, polyether, polypropylene oxide, polyepichlorohydrin,
  • Polyhydroxyacetic acid Polyethylene terephthalate, polybutylene terephthalate,
  • Polyhydroxybenzoate polyhydroxypropionic acid, polypivalolactone, polycaprolactone,
  • Polymeric C-S bonds in the main chain for example polysulfide ether,
  • Polyimines polyisocyanides, polyetherimine, polyetherimides, polyaniline, polyaramides,
  • Liquid crystalline polymers especially Vectra as well
  • Inorganic polymers for example polysilanes, polycarbosilanes, polysiloxanes,
  • Polysilicic acid Polysilicates, silicones, polyphosphazenes and polythiazyl.
  • high-temperature stable polymers which contain at least one nitrogen, oxygen and / or sulfur atom in one or in different repeating units.
  • High-temperature stable in the sense of the present invention is a polymer which, as a polymer electrolyte, can be operated continuously in a fuel cell at temperatures above 120 ° C.
  • Permanently means that a membrane according to the invention can be operated for at least 100 hours, preferably at least 500 hours at at least 120 ° C., preferably at least 160 ° C., without the performance that can be measured according to the method described in WO 01/18894 A2, decreases by more than 50% based on the initial output.
  • the polymers used to produce the films are preferably polymers which have a glass transition temperature or Vicat Softening temperature VST / A / 50 of at least 100 ° C, preferably at least 150 ° C and most preferably at least 180 ° C.
  • Polymers which contain at least one nitrogen atom in a repeating unit are particularly preferred. Particularly preferred are polymers which contain at least one aromatic ring with at least one nitrogen 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. According to a particular aspect of the present invention, preferred molded articles comprising polymers, in particular polymer films, comprise at least 80% by weight, in particular at least 90% by weight, of polyazoles.
  • 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 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 (XIII) and / or (XIV) and / or (XV) and / or (XVI) and / or (XVII) and / or (XVIII) and / or (XIX) and / or (XX) and / or (XXII) and / or (XVIII) and / or (XIX) and / or (XX) and / or (XXI) and / or (XVIII) and / or (XIX) and / or (XX) and / or (XXI) and / or (XXII)
  • 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-bonded aromatic or heteroaromatic group, which may be single or multi-membered
  • Ar 6 are the same or different and for a double-bonded aromatic or heteroaromatic group, which can be mononuclear or polynuclear
  • Aromatic or heteroaromatic groups preferred according to the invention are derived from benzene, naphthalene, biphenyl, diphenyl ether, diphenyl methane, diphenyldimethyl methane, bisphenone, diphenyl sulfone, 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-triazole, 1, 2,3,4-tetrazole, benzo [b] thiophene,
  • 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 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.
  • 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.
  • 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.
  • 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, segmented copolymers and / or alternating polymers.
  • 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 100 repeating azole units.
  • polymers containing recurring benzimidazole units are preferred.
  • Some examples of the extremely useful polymers containing repeating benzimidazole units are given by the following formulas:
  • n and m is an integer greater than or equal to 10, preferably greater than or equal to 100.
  • the preferred polyazoles but especially the polybenzimidazoles, are notable for their high molecular weight. Measured as intrinsic viscosity, this is preferably at least 0.2 dl / g, in particular 0.8 to 10 dl / g, particularly preferably 1 to 5 dl / g.
  • polyazole polymers are polyimidazoles, polybenzthiazoles, polybenzoxazoles, polytriazoles, polyoxadiazoles, polythiadiazoles, polypyrazoles, polyquinoxalines, poly (pyridines), poly (pyrimidines), and poly (tetrazapyrenes).
  • Preferred polybenzimidazoles are commercially available under the trade name ⁇ Celazole from Celanese AG.
  • the preferred polymers include polysulfones, in particular polysulfones aromatic and / or heteroaromatic groups in the main chain.
  • preferred polysulfones and polyether sulfones have a melt volume rate MVR 300/21, 6 is less than or equal to 40 cm 3/10 min, especially less than or equal to 30 cm 3/10 min and particularly preferably less than or equal to 20 cm 3 / 10 min measured according to ISO 1133.
  • Polysulfones with a Vicat softening temperature VST / A / 50 of 180 ° C. to 230 ° C. are preferred.
  • the number average molecular weight of the polysulfones is greater than 30,000 g / mol.
  • Polysulfone-based polymers include, in particular, polymers which have recurring units with linking Suifon groups corresponding to the general formulas A, B, C, D, E, F and / or G:
  • radicals R independently of one another, represent the same or different aromatic or heteroaromatic groups, these radicals being explained in more detail above. These include in particular 1, 2-phenylene, 1, 3-phenylene, 1, 4-phenylene, 4,4'-biphenyl, pyridine, quinoline, naphthalene, phenanthrene.
  • polysulfones preferred in the context of the present invention include homopolymers and copolymers, for example statistical copolymers.
  • Particularly preferred polysulfones comprise repeating units of the formulas H to N: (H) K HHQ
  • the polysulfones described above can be obtained commercially under the trade names Victrex 200 P, ® Victrex 720 P, ® Ultrason E, ® Ultrason S, ® Mindel, ® Radel A, ® Radel R, ® Victrex HTA, ® Astrel and ® Udel.
  • polyether ketones polyether ketone ketones
  • polyether ether ketones polyether ketone ketones
  • polyaryl ketones are particularly preferred. These high-performance polymers are known per se and can be obtained commercially under the trade names Victrex® PEEK TM, ® Hostatec, ® Kadel.
  • polymers can also be used, the acid groups contain.
  • These acid groups include, in particular, sulfonic acid groups.
  • Polymers with aromatic sulfonic acid groups can preferably be used here.
  • 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.
  • 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.
  • the polymers modified with sulfonic acid groups preferably have a sulfonic acid group content in the range from 0.5 to 3 meq / g. This value is determined via the so-called ion exchange capacity (IEC).
  • IEC ion exchange capacity
  • the sulfonic acid groups are converted into the free acid.
  • 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 h. 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 containing sulfonic acid groups can be prepared, for example, by sulfonating 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).
  • non-fluorinated polymers were developed by sulfonation of high-temperature stable thermoplastics.
  • sulfonated polyether ketones DE-A-4219077, WO96 / 01177
  • sulfonated polysulfones J. Membr. Be. 83 (1993) p.211
  • sulfonated polyphenylene sulfide DE-A-19527435
  • US-A-6110616 describes copolymers of butadiene and styrene and their subsequent sulfonation for use in fuel cells.
  • perfluorinated polymers as described in US-A-5422411 can be prepared by copolymerization from trifluorostyrene and sulfonyl-modified trifuorostyrene.
  • the preferred polymers having acid groups include sulfonated polyether ketones, sulfonated polysulfones, sulfonated polyphenylene sulfides, perfluorinated polymers containing sulfonic acid groups, as described in US-A-3692569, US-A-5422411 and US-A-6110616.
  • Blends containing polyazoles and / or polysulfones are particularly preferred.
  • the use of blends can improve the mechanical properties and reduce the material costs.
  • the molded body comprising the polymers for example the polymer film
  • the polymer film used for swelling comprising a basic polymer and at least one blend component, additionally contains a crosslinking agent as described in German patent application No. 10140147.7.
  • polymer film used for the treatment is previously treated as described in German Patent Application No. 10109829.4.
  • This variant is advantageous in order to increase the absorption capacity of the polymer film in relation to the monomers comprising phosphonic acid groups.
  • the polymers set out above can be extruded, among other things.
  • Polymer films are also available by casting processes. For example, polyazoles can be dissolved in polar, aprotic solvents such as dimethylacetamide (DMAc) and a film can be produced using conventional methods.
  • DMAc dimethylacetamide
  • the film thus obtained can be treated with a washing liquid in a first step.
  • This washing liquid is preferably selected from the group of alcohols, ketones, alkanes (aliphatic and cycloaliphatic), ethers (aliphatic and cycloaliphatic), esters, carboxylic acids, where the above group members can be halogenated, water, inorganic acids (such as H3P04, H2S04) and mixtures thereof.
  • C1-C10 alcohols C2-C5 ketones, C1-C10 alkanes (aliphatic and cycloaliphatic), C2-C6 ethers (aliphatic and cycloaliphatic), C2-C5 esters, C1-C3 carboxylic acids, dichloromethane, water, inorganic acids (such as H3P04, H2S04) and mixtures thereof.
  • water is particularly preferred.
  • the liquid which is used in a first step comprises at least 70% by weight of water. After the polymer film has been washed, the treatment liquid is changed.
  • the film can be dried to remove the washing liquid. Drying takes place depending on the partial vapor pressure of the selected treatment liquid. Usually drying takes place at normal pressure and temperatures between 20 ° C and 200 ° C. A more gentle drying can also be done in a vacuum. Instead of drying, the membrane can also be dabbed off, thus removing excess treatment liquid. The order is not critical.
  • the mechanical properties of the film are surprisingly improved by cleaning the polymer film, in particular the polyazole film, from solvent residues as described above. These properties include in particular the modulus of elasticity, the tensile strength and the fracture toughness of the film. Furthermore, contamination of the treatment liquid by released solvent residues can thereby be avoided.
  • these films are doped with a monomer comprising phosphonic acid groups and / or monomers comprising sulfonic acid groups.
  • Monomers comprising phosphonic acid groups and / or 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 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.
  • 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 can contain one, two, three or more phosphonic acid groups.
  • 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 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 with halogen, -OH, COOZ, -CN, NZ 2 can be substituted,
  • Z independently of one another hydrogen, 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 by 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 and / or of the formula x (Z 2 0 3 P) -R- -R— (P o 3 Z 2 ) x where
  • 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 with halogen, -OH, COOZ, -CN, NZ 2 can be substituted,
  • A represents a group of the formulas COOR 2 , CN, CONR 2 2 , OR 2 and / or R 2 , where 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
  • 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 with 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 means.
  • the preferred monomers comprising phosphonic acid groups include inter alia alkenes which have phosphonic acid groups, such as ethenephosphonic acid, propenephosphonic acid, butenephosphonic acid; Acrylic acid and / or methacrylic acid compounds that have phosphonic acid groups, such as 2-phosphonomethyl-acrylic acid, 2-phosphonomethyl-methacrylic acid, 2-phosphonomethyl-acrylic acid amide and 2-phosphonomethyl-methacrylic acid amide.
  • vinylphosphonic acid ethenephosphonic acid
  • 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.
  • derivatives include in particular the salts, the esters, the amides and the halides of the monomers comprising phosphonic acid groups.
  • the liquid used for the treatment 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, of monomers comprising phosphonic acid groups and / or monomers comprising sulfonic acid groups.
  • the liquid used for the treatment 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.
  • DMSO dimethyl sulfoxide
  • esters such as ethyl acetate
  • polar protic solvents such as alcohols such as ethanol, propanol, isopropanol and / or butanol.
  • the inorganic solvent includes in particular water, phosphoric acid and polyphosphoric acid.
  • the absorption capacity of the film in relation to the monomers can be improved by adding the organic solvent.
  • the content of monomers comprising phosphonic acid groups and / or monomers comprising sulfonic 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.
  • 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.
  • 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.
  • 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
  • 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 with halogen, -OH, COOZ, -CN, NZ 2 can be substituted,
  • Z independently of one another is 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, 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
  • 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 with halogen, -OH, COOZ, -CN, NZ 2 can be substituted,
  • Z independently of one another is hydrogen, C1-C15-alkyl group, C1-C15-alkoxy group, ethyleneoxy group or C5-C20-aryl or heteroaryl group, where the above radicals in turn can be substituted by halogen, -OH, -CN, and x is an integer 1, 2, 3, 4, 5, 6, 7, 8, 9 or 10 means
  • 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
  • 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 with 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 means.
  • the preferred monomers comprising sulfonic acid groups include other 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.
  • vinyl sulfonic acid ethene sulfonic acid
  • 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.
  • derivatives include in particular the salts, the esters, the amides and the halides of the monomers comprising sulfonic acid groups.
  • 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.
  • the monomers comprising phosphonic acid groups are preferred over the monomers comprising sulfonic acid groups. Accordingly, a liquid is particularly preferably used which has monomers comprising phosphonic acid groups.
  • monomers capable of crosslinking can be used in the production of the polymer membrane. These monomers can be added to the liquid used to treat the film. In addition, the monomers capable of crosslinking can also be applied to the flat structure after treatment with the liquid.
  • 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.
  • 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 ester, nitrile, amine, silyl, siloxane radicals.
  • 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.
  • Ebacryl N ', N-methylenebisacrylamide
  • carbinol, butadiene isoprene, chloroprene, divinylbenzene and / or bisphenol A dimethylacrylate.
  • crosslinking agents are 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 phosphonic comprehensive monomers can be used.
  • the liquid containing monomers comprising phosphonic acid groups and / or monomers comprising sulfonic 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 and / or monomers comprising sulfonic acid groups can be in wide ranges, 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 shaped body comprising polymers is passed through a liquid-filled trough at least twice, the shaped body comprising polymers being unwound from a spool and wound onto a further spool, and the direction of travel of the shaped body comprising a polymer during the treatment Changing the direction of rotation of the coils changes.
  • the shaped body for example a film, is passed through a liquid bath at least twice, preferably at least 10 times and particularly preferably at least 25 times, the direction of rotation of the film being changed by changing the direction of rotation of the coils.
  • the speed at which the shaped body is guided through the liquid depends on the type of liquid and the shaped body. In general, the molded body is drawn through the liquid bath at a speed of 0.5 to 100 m / min, in particular 1.0 to 25 m / min.
  • the immersion path of the shaped body in the liquid is preferably 0.05 to 10 m, in particular 0.15 m to 2 m.
  • the total treatment time is in the range from 2 minutes to 10 hours, preferably in the range from 15 minutes to 3 hours.
  • the speed at which the molded body is guided through the liquid bath can be controlled in a manner known per se. This includes, among other things a control of the rotational speed of the coils via a tachometer roller or by measuring their speed.
  • the molded body is subjected to a retraction force during the treatment.
  • a retraction force in the range from 0.1 to 400 N, in particular 0.2 to 300 N and particularly preferably 2.4 to 120 N, without any intention that this should impose a restriction.
  • a film with a retraction force based on the width of the film is preferably in the range from 0.5 to 200 N / m, preferably from 1 to 150 N / m and particularly preferably in the range from 12 to 60 N / m, through the trough filled with liquid guided.
  • the width here refers to the linear expansion of the film perpendicular to the running direction before treatment with liquid. Based on film with a width in the range from 20 cm to 200 cm, this results in preferred retraction forces in the range from 0.1 to 400 N, in particular 0.2 to 300 N and particularly preferably 2.4 to 120 N, without this resulting in a Restriction should take place.
  • liquid adheres to the film, preferably at least 1 g / m 2 , in particular at least 10 g / m 2, of liquid treatment remaining on the film.
  • This value relates to the weight gain due to the treatment with liquid, based on the weight of a dry film which has been freed from solvent residues by at least one washing step.
  • a washing liquid for example water, preferably 1 to 1000 ml / m 2 , in particular 5 to 250 ml / m 2 , particularly preferably 15 to 150 ml / m 2 and very particularly preferably 25 to 75 ml / m 2 adhere on the slide.
  • Excess liquid can optionally be removed, for example with a roller.
  • the film is doped with monomers comprising phosphonic acid groups and / or monomers comprising sulfonic acid groups, then preferably 1 to 1000 ml / m 2 , in particular 10 to 800 ml / m 2 , particularly preferably 50 to 600 ml / m 2 and very particularly preferably 100 to 400 ml / m 2 on the film
  • the amount of liquid that adheres to and penetrates the film after treatment in the liquid bath can be controlled via the speed at which the film is passed through the liquid bath.
  • the amount of liquid depends on the temperature at which the treatment takes place.
  • the temperature at which the present process is carried out is not critical and can therefore vary within wide limits, generally avoiding polymerization of the monomers in the tub.
  • the present method is preferably carried out in the range from 0 to 150 ° C., preferably 10 ° C. to 100 ° C., the ranges depending on the physical properties of the liquid.
  • the liquid in the tub can be renewed or replaced by another liquid as required.
  • a dirty liquid can be replaced by a fresh liquid of the same type.
  • the liquid can be exchanged for another.
  • a film can be washed as well as doped without the need to use another device. This process can be carried out batchwise or continuously, and individual components can also be metered in.
  • the liquid can be circulated in the tub in order to ensure the homogeneity of the liquid, so that, for example, a change in the composition is avoided.
  • Jiggers which are described, for example, in Dietmar Fries, Training Aids, Teaching Aids "Textile Finishing, Coating", Employers' Group for All Textile AGK (1992) p. 2.13, are particularly suitable for carrying out the present method. These devices can be obtained from Mathis AG and Kuester AG, among others can be obtained commercially.
  • a polymer film (1) for example a polyazole film
  • a polyazole film is unwound from a spool (2) and wound onto a second spool (3) and is guided, for example, over a roller (4).
  • the film is passed through a tub (5) and there over a Roller (6) deflected.
  • the film is treated with liquid in the tub. After leaving the trough followed by a further deflection, excess liquid can optionally be removed by pressure generated by a further roller (7) before winding up. Liquid generally adheres to the polyazole films, so that this liquid acts on the film even in the wound state.
  • All parts of the jigger that come into contact with the liquid can be rustproof. It is particularly preferred to use jiggers whose parts, such as rollers, coils, etc., are coated with stable plastics, for example perfluorinated polymers, polyether ketone and polyether sulfone, in particular ⁇ Etlon. This is particularly advantageous for doping the film with concentrated acids. Accordingly, the rollers and coils can be made of stainless steel, for example.
  • the speed and / or the retraction force of the film can be determined, for example, using the rollers (4) and / or (6), which is then designed as a tachometer or tensiometer roller.
  • the device can be equipped with an electronic control that regulates the speed and direction of the rollers. It can be provided that the device automatically changes the running direction after the entire film (1) has been transferred from one spool (2) to the second spool (3).
  • means for temperature control of the jigger in particular the trough (5), can be provided, the thermal energy introduced into the rolled-up film also depending in particular on the rotational speed of the coils (2) and (3).
  • the jigger can comprise a cover (8) which seals off the tub and the coils from the surroundings. This can prevent the liquid from volatilizing. Furthermore, hygroscopic liquids, such as concentrated phosphoric acid, can be protected from moisture, and the jigger can be flushed with dry air or with nitrogen.
  • 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 be done, for example, by adding to the liquid, which the Contains monomers comprising phosphonic acid groups and / or monomers comprising sulfonic acid groups.
  • these additives are in liquid form, they can also be added after the monomers have been polymerized.
  • 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 P0 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 0 8 , HSb 3 P 2 0 14 , H 5 Sb 5 p2 ⁇ 2
  • Oxides such as Al 2 0 3 , Sb 2 0 5 , Th0 2 , Sn0 2 , Zr0 2 , Mo0 3
  • Silicates such as zeolites, layered silicates, framework silicates, H-natrolites, H-mordenites, NH 4 -analcines, NH 4 -sodalites, NH 4 -galates, H-montmorillonites, acids such as HCI0 4 , SbFs fillers such as carbides, especially SiC, Si 3 N 4 , fibers, in particular glass fibers, glass powders and / or polymer fibers, preferably based on polyazoles.
  • the membrane comprises at most 80% by weight, preferably at most 50% by weight and particularly preferably at most 20% by weight of additives after the polymerization.
  • 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 adsorption of phosphoric acid and phosphate to platinum.
  • perfluorinated sulfonic acid additives preferably 0.1-20% by weight, preferably 0.2-15% by weight, very preferably 0.2-10% by weight.
  • Non-limiting examples of perfluorinated sulfonic acid additives are: trifluoromethanesulfonic acid, potassium trifluoromethanesulfonate, sodium trifluoromethanesulfonate, lithium, Ammoniumtrifluormethansulfonat, Kaliumperfluorohexansulfonat, Natriumperfluorohexansulfonat perfluorohexanesulphonate, lithium, ammonium perfluorohexanesulphonate, perfluorohexanesulphonic acid, potassium nonafluorobutanesulphonate, Natriumnonafluorbutansulfonat, Lithiumnonafluorbutansulfonat, Ammoniumnonafluorbutansulfonat, Cäsiumnonafluorbutansulfonat, Triethylammoniumperfluorohexasulfonat and Perfluorsulfoimide.
  • the monomers contained in the film can be polymerized.
  • the polymerization of the monomers comprising phosphonic acid groups is preferably carried out by free radicals.
  • the radical formation can take place thermally, photochemically, chemically and / or electrochemically.
  • a starter solution can be applied to the monomers after treatment with the liquid containing monomers comprising phosphonic acid groups and / or monomers comprising sulfonic acid groups. This can be done by means of measures known per se (e.g. spraying, dipping, etc.) which are known from the prior art.
  • a starter solution can be added to the liquid containing monomers comprising phosphonic acid groups and / or monomers comprising sulfonic acid groups.
  • 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- (isobutterklamidin ) hydrochloride, benzpinacol, dibenzyl derivatives, Methyl ethylene ketone peroxide, 1, 1-azobiscyclohexane carbonitrile, methyl ethyl ketone peroxide, acetylacetone peroxide, dilauryl peroxide, didecanoyl peroxide, tert-butyl per-2-ethylhexanoate
  • radical formers can also be used which form radicals when irradiated.
  • the preferred compounds include ⁇ , ⁇ -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 ( ⁇ Irgacure 819) and 1- [4- (2-hydroxyethoxy) phenyl] -2-hydroxy-2-phenylpropan-1-one ( ⁇ Irgacure 2959), each from Ciba Geigy Corp. are commercially available.
  • radical formers 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 to radical formers.
  • the amount of radical generator can be varied depending on the desired degree of polymerization.
  • 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).
  • a damp film can also be irradiated here.
  • drying also results from the radiation.
  • 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, ⁇ .auflage, Volume 1, p.492-511; DR Arnold, NC Baird, JR Bolton, JCD Brand, PW M Jacobs, P.de Mayo, WR Ware, Photochemistry-An Introduction, Academic Press, New York and MKMishra, Radical Photopolymerization of Vinyl Monomers, J. Macromol. Sci.-Revs. Macromol. Chem. Phys. C22 (1982-1983) 409.
  • 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 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 membrane before the polymerization.
  • the membranes have high mechanical stability. This size results from the hardness of the membrane, which is determined by means of microhardness measurement in accordance with DIN 50539.
  • 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.
  • 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 any intention that this should impose a restriction.
  • the force is then kept constant at 3 mN for 5 s and the creep is calculated from the penetration depth.
  • 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 is YHU at least 0.5 MPa, in particular at least 5 MPa and very particularly preferably at least 10 MPa, without this being intended to impose a restriction.
  • the flat structure which is obtained after the polymerization is a self-supporting membrane.
  • the degree of polymerization at least 2, in particular at least 5, particularly preferably at least 30 repeating units, in particular at least 50 repeating units, very particularly preferably at least 100 repeating units.
  • M n the number average molecular weight
  • M n the number average molecular weight
  • the proportion by weight of monomer 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.
  • preferred membranes comprise portions of low molecular weight polymers comprising phosphonic acid groups.
  • the polymerization can lead to a decrease in the layer thickness.
  • the thickness of the self-supporting membrane is preferably between 15 and 1000 ⁇ m, preferably between 20 and 500 ⁇ m, in particular between 30 and 250 ⁇ m.
  • the stability of the film must not fall below a value that depends on the device used.
  • the polymerization of the monomers increases the stability of the film, so that the doping process can be repeated, for example to increase the phosphonic acid group content of the polymer membrane.
  • a combination of the treatment step with the liquid which has monomers comprising phosphonic acid groups and / or monomers comprising sulfonic acid groups and subsequent polymerization of the monomers can be carried out at least twice, preferably at least 4 times and particularly preferably at least 6 times.
  • 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.
  • 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.
  • Another method is radiation with ⁇ , ⁇ 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.
  • 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.
  • 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.
  • 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).
  • IEC ion exchange capacity
  • the phosphonic acid groups are converted into the free acid, the measurement being carried out before polymerization of the monomers comprising phosphonic acid groups.
  • 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 obtainable by the present method has improved material properties compared to the previously known doped polymer membranes. In particular, they perform better than known doped polymer membranes. This is based in particular on an improved, intrinsic proton conductivity, which is based in particular on polymers containing phosphonic acid groups. 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.
  • 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.
  • a membrane can be moistened at low temperatures.
  • the compound used as an energy source for example hydrogen
  • 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-redoped membrane is measured immediately before sample assembly. To measure the temperature dependency, the measuring cell is brought to the desired temperature in an oven, which is controlled by 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 is preferably less than 100 mA / cm 2 , in particular less than 50 mA / cm 2, very particularly preferably less than 10 mA / cm 2 .
  • the amount of carbon dioxide released at the cathode is measured using 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.
  • the intrinsically conductive polymer membranes Possible areas of application of the intrinsically conductive polymer membranes include uses in fuel cells, in electrolysis, in capacitors and in battery systems. Due to their property profile, the polymer membranes can preferably be used in fuel cells, in particular in DMBZ Fuel cells (direct methanol fuel cell) can be used.
  • preferred anisotropic shaped bodies are membranes which can be used, for example, for microfiltration, ultrafiltration, reverse osmosis, electrodialysis and pervaporation.
  • These moldings can be obtained in particular by removing the monomers comprising phosphonic acid groups after the treatment with the liquid. This can be achieved, for example, by washing with the washing liquids shown above.
  • the shape of part of the pores of preferred membranes is anisotropic. Accordingly, these pores do not have a round shape, but a shape that has different dimensions in height and width.
  • the width of these pores is preferably in the range from 1.5 nm to 700 nm, in particular in the range from 8 nm to 400 nm and particularly preferably 15 nm to 200 nm.
  • the height of these pores is preferably in the range from 1 nm to 500 nm, in particular in the range from 5 nm to 300 nm and particularly preferably 10 nm to 150 nm. In a two-dimensional approach, the width is understood as the greatest length extension of the pore and the height as the minimum length extension of the pore.
  • the ratio of width to height is preferably in the range from 1.2 to 20, in particular in the range from 1.5 to 10 and particularly preferably in the range from 2 to 5.
  • These variables can be determined in particular by transmission electron microscopy (TEM) or atomic force microscopy (AFM) become.
  • At least 70%, particularly preferably at least 80% of the pores preferably have an anisotropic shape.
  • An anisotropic molded article of the present invention for example a membrane for microfiltration, ultrafiltration, etc. or a proton-conducting polymer electrolyte membrane, which can be used in particular in fuel cells, preferably has a maximum modulus of elasticity of at least 50 MPa, in particular at least 100 MPa and particularly preferably at least 150 MPa.
  • the ratio of maximum modulus of elasticity to minimum modulus of elasticity is preferably at least 1.5, in particular at least 1.8, and particularly preferably at least 2.1.
  • the maximum modulus of elasticity generally results from the value measured in the direction of the load, whereas the minimum value results from the value perpendicular to the direction of the load.
  • the loading direction refers to the direction in which the train is wound up a spool is applied according to the present method.
  • the modulus of elasticity can be determined in accordance with the tensile elongation tests described in German patent application application number 10129458.1.
  • a 10 m long and 36 cm wide PBI film with a thickness of 55 ⁇ m was introduced at 70 ° C. through a tub filled with 5L 90% aqueous vinylphosphonic acid (VPA).
  • the film is guided by a spool at a speed of 3 m / min and unwinded with a restoring force of 0.63 N / cm and spooled onto another spool.
  • the direction of travel of the PBI film was changed during the treatment by changing the direction of rotation of the coils.
  • the film was doped for a total of 3 hours.
  • the thickness of the film was 105 ⁇ m after the doping.
  • the doped film was then irradiated with an irradiation dose of 99 kJ / kg.

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)
  • Fuel Cell (AREA)
  • Treatments Of Macromolecular Shaped Articles (AREA)

Abstract

L'invention concerne un procédé pour produire des corps moulés anisotropes, selon lequel un corps moulé comprenant un polymère est dirigé à travers un réservoir rempli de liquide présentant un composé qui comporte au moins deux atomes de carbone, le polymère n'étant pas dévidé d'une bobine de polymères ou pouvant être dévidé d'une autre bobine. Le liquide comprend des groupes d'acide phosphorique et/ou des monomères comprenant de l'acide sulfurique.
EP05760686A 2004-05-14 2005-05-13 Corps moule anisotrope, procede pour produire et utiliser des corps moules anisotropes Withdrawn EP1747248A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102004024169 2004-05-14
PCT/EP2005/005283 WO2005111123A1 (fr) 2004-05-14 2005-05-13 Corps moule anisotrope, procede pour produire et utiliser des corps moules anisotropes

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EP1747248A1 true EP1747248A1 (fr) 2007-01-31

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EP05760686A Withdrawn EP1747248A1 (fr) 2004-05-14 2005-05-13 Corps moule anisotrope, procede pour produire et utiliser des corps moules anisotropes

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US (1) US20070203252A1 (fr)
EP (1) EP1747248A1 (fr)
JP (1) JP2007537317A (fr)
KR (1) KR20070067649A (fr)
CN (1) CN1997690A (fr)
WO (1) WO2005111123A1 (fr)

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US3692569A (en) * 1970-02-12 1972-09-19 Du Pont Surface-activated fluorocarbon objects
US4453991A (en) 1981-05-01 1984-06-12 E. I. Du Pont De Nemours And Company Process for making articles coated with a liquid composition of perfluorinated ion exchange resin
US5422411A (en) 1993-09-21 1995-06-06 Ballard Power Systems Inc. Trifluorostyrene and substituted trifluorostyrene copolymeric compositions and ion-exchange membranes formed therefrom
GB9413417D0 (en) 1994-07-04 1994-08-24 Ford Roger A Improved composite materials and method for making them
DE19527435A1 (de) 1995-07-27 1997-01-30 Hoechst Ag Polymerelektrolyte und Verfahren zu deren Herstellung
US6248469B1 (en) * 1997-08-29 2001-06-19 Foster-Miller, Inc. Composite solid polymer electrolyte membranes
US6110616A (en) 1998-01-30 2000-08-29 Dais-Analytic Corporation Ion-conducting membrane for fuel cell
JP2000281819A (ja) 1999-01-27 2000-10-10 Aventis Res & Technol Gmbh & Co Kg 架橋高分子膜の製造方法及び燃料電池
EP1523053A3 (fr) 1999-09-09 2010-04-28 Danish Power Systems APS Piles à combustible à membrane polymérique comme électrolyte
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Publication number Publication date
KR20070067649A (ko) 2007-06-28
JP2007537317A (ja) 2007-12-20
CN1997690A (zh) 2007-07-11
US20070203252A1 (en) 2007-08-30
WO2005111123A1 (fr) 2005-11-24

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