US20100063168A1
2010-03-11
11/573,982
2005-08-20
The invention relates to ionomeric membranes, comprising a non- or partly-fluorinated, non-, partly- or fully-aromatic backbone and a non- or partly-fluorinated sidechain with ionogenic groups, or the non-ionic precursors thereof and a method for production of said ionomeric membranes.
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H01M8/0289 » CPC main
Fuel cells; Manufacture thereof; Details Means for holding the electrolyte
B01D67/0006 » CPC further
Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus; Organic membrane manufacture by chemical reactions
B01D67/0093 » CPC further
Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus; After-treatment of organic or inorganic membranes Chemical modification
B01D71/68 » CPC further
Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor; Organic material; Polymers having sulfur in the main chain, with or without nitrogen, oxygen or carbon only Polysulfones; Polyethersulfones
B01D71/82 » CPC further
Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor; Organic material; Macromolecular material not specifically provided for in a single one of groups  - characterised by the presence of specified groups, e.g. introduced by chemical after-treatment
B01J39/19 » CPC further
Cation exchange; Use of material as cation exchangers; Treatment of material for improving the cation exchange properties; Use of material as cation exchangers; Treatment of material for improving the cation exchange properties; Organic material; Macromolecular compounds obtained otherwise than by reactions only involving unsaturated carbon-to-carbon bonds
C08G65/48 » CPC further
Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from hydroxy compounds or their metallic derivatives Polymers modified by chemical after-treatment
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Macromolecular compounds obtained by reactions forming a linkage containing sulfur with or without nitrogen, oxygen, or carbon in the main chain of the macromolecule; Polythioethers; Polyarylenethioethers Chemical after-treatment
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Manufacture of articles or shaped materials containing macromolecular substances; Manufacture of shaped structures of ion-exchange resins; Films, membranes or diaphragms based on organic and/or inorganic macromolecular compounds; Synthetic macromolecular compounds based on macromolecular compounds obtained by reactions involving unsaturated carbon-to-carbon bonds
C08J5/2256 » CPC further
Manufacture of articles or shaped materials containing macromolecular substances; Manufacture of shaped structures of ion-exchange resins; Films, membranes or diaphragms based on organic and/or inorganic macromolecular compounds; Synthetic macromolecular compounds based on macromolecular compounds obtained by reactions other than those involving carbon-to-carbon bonds, e.g. obtained by polycondensation
H01M8/1023 » CPC further
Fuel cells; Manufacture thereof; Fuel cells with solid electrolytes characterised by the electrolyte material; Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer having only carbon, e.g. polyarylenes, polystyrenes or polybutadiene-styrenes
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Fuel cells; Manufacture thereof; Fuel cells with solid electrolytes characterised by the electrolyte material; Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer having only carbon and oxygen, e.g. polyethers, sulfonated polyetheretherketones [S-PEEK], sulfonated polysaccharides, sulfonated celluloses or sulfonated polyesters
H01M8/1027 » CPC further
Fuel cells; Manufacture thereof; Fuel cells with solid electrolytes characterised by the electrolyte material; Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer having carbon, oxygen and other atoms, e.g. sulfonated polyethersulfones [S-PES]
H01M8/103 » CPC further
Fuel cells; Manufacture thereof; Fuel cells with solid electrolytes characterised by the electrolyte material; Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer having nitrogen, e.g. sulfonated polybenzimidazoles [S-PBI], polybenzimidazoles with phosphoric acid, sulfonated polyamides [S-PA] or sulfonated polyphosphazenes [S-PPh]
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Fuel cells; Manufacture thereof; Fuel cells with solid electrolytes characterised by the electrolyte material; Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer having sulfur, e.g. sulfonated-polyethersulfones [S-PES]
H01M8/1039 » CPC further
Fuel cells; Manufacture thereof; Fuel cells with solid electrolytes characterised by the electrolyte material; Polymeric electrolyte materials halogenated, e.g. sulfonated polyvinylidene fluorides
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Fuel cells; Manufacture thereof; Fuel cells with solid electrolytes characterised by the electrolyte material; Polymeric electrolyte materials characterised by the manufacturing processes by chemical reactions, e.g. polymerisation or crosslinking
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Details relating to properties of membranes Membrane materials having positively charged functional groups
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Characterised by the use of macromolecular compounds obtained by reactions forming a carbon-to-carbon link in the main chain ; Derivatives of such polymers Polyphenylenes
C08J2381/06 » CPC further
Characterised by the use of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing sulfur with or without nitrogen, oxygen, or carbon only; Polysulfones; Derivatives of such polymers Polysulfones; Polyethersulfones
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Electrolytes; Non-aqueous electrolytes; Solid electrolytes Organic polymers
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Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation; Hydrogen technology Fuel cells
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Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation; Hydrogen technology Fuel cells
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Climate change mitigation technologies in the production process for final industrial or consumer products Manufacturing or production processes characterised by the final manufactured product
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Climate change mitigation technologies in the production process for final industrial or consumer products Manufacturing or production processes characterised by the final manufactured product
B01J39/18 IPC
Cation exchange; Use of material as cation exchangers; Treatment of material for improving the cation exchange properties; Use of material as cation exchangers; Treatment of material for improving the cation exchange properties; Organic material Macromolecular compounds
It is claimed:
Ionomer membranes containing phosphoric acid or phosphonic acid have received in recent years a growing interest because the phosphoric and phosphonic acid groups show water-free proton conductivity, in that phosphoric acid groups or phosphonic acid groups can act as proton donator as well as as proton acceptor. This water-free proton conductivity of phosphoric acids is especially interesting for fuel cells in the temperature range between 100° C. and 200° C., because in this temperature range in fuel cells the vapour pressure of water is very low so that sulfonic acid containing ionomer membranes do not work anymore, because they need water molecules as proton acceptors. From the literature several membrane types are known, whose proton conductivity is generated from phosphoric acid or phosphonic acids.
There are for example:
For sulfonated ionomers it ha been shown, that the arrangement of the sulfonic acid groups in the side chain results in an increase in proton conductivity above 100° C. as compared with sulfonated ionomers with the sulfonic acid groups in the aromatic main chain. In a specific example the proton conductivities of sulfonated PEEK (sPEEK) and of poly(carbonylphenoxy)phenylene (âPoly-X 2000â) at 120° C. have been compared5. The Poly-X 2000 polymer was at 120° C. much more proton conducting than sPEEK. Disadvantages of this polymer are the expensive production process and the great stiffness of the polymer main chain and side chain. 5N. Ogato, M. Rikukawa, WO 94/24717
The aim of the invention is to provide ionomers and ionomer membranes with the ionic group on a flexible side chain which has a positive impact on the proton conductivity of the ionomers. The aim is furthermore to provide processes for the production of these polymeric proton conductors.
Ionomers according to the invention are shown in FIG. 1.
Surprisingly it has been found that ionomers and ionomer membranes with ionic groups or their non-ionic precursors at the end of a flexible side chain can be obtained by method 1 with the following steps:
The method 1 is depicted in FIG. 2.
Surprisingly it has been found that also method 2 leads to ionomers and ionomer membranes with a proton conducting group in the side chain:
The method 2 is depicted in FIG. 3.
Surprisingly it has been found that the side chain halogenated polymers can be converted via Michaelis-Arbusov reaction or related reactions and subsequent hydrolysis towards polymers with the phosphonic acid group in the side chain. This reaction is depicted in FIG. 4.
As polymer main chains all kinds of polymers are possible. Preferred as main chains are however:
Particularly preferred are (Het)aryl main chain polymers like:
Suitable reagents for the deprotonation of the aryl polymer are n-butyllithium, sec-butyllithium, tert. butyllithium, methyllithium, phenyllithium, Grignard compounds like phenylmagnesiumhalide and other Grignard compounds, lithium diisopropylamide, and other lithium amides, sodium naphtalide, potassium naphtalide, zinc organic compounds (âRieke metalsâ)
Suitable solvents for the metal organic reaction are ether solvents like THF, diethylether, glyme, diglyme, triglyme, dioxane and other ether solvents as well as hydrocarbon solvents CnH2n+2, cyclohexane, benzene, toluene, xylole and other CâHâ aromatic solvants and any other mixtures thereof and with ether solvents.
Some of the suitable compounds with nucleophilically substitutable halogens and ionogenic groups or their non-ionic precursors for the reaction with the deprotonated polymers are depicted in FIG. 2. Particularly preferred are compounds of the typ Hal-(CH2)xâY (Y see FIG. 2, x=1â20).
The compounds with nucleophilically substitutable halogens and ionogenic groups may contain as halogene F, Cl, Br, or I. Preferred are Cl, Br and I. Also mixtures of organic compounds with different halgenes and different alkyl chain lengths can be used.
Suitable dihalogene compounds for the reaction with the deprotonated polymers are: Hal-(C(R1)2)x-Hal Cl, Br, I; R1=H, F, CnH2n+1, aryl). The dihalogen alcanes according to the invention method 2 can be also mixed dihalogen alcanes, that is compounds like Brâ(C(R1)2)xâI, where both halogen atoms have different reactivity to assure that no cross-linking takes place during method 2. If for example the compound Iâ(CH2)âCl is reacted with lithiated PSU, I is preferred to be exchanged nucleophilically. Thereby Cl, Br and I are preferred. Also mixtures of dihalogene compounds with different halgenes and different alkyl chain lengths can be used. Also compounds like Hal-(C(R1)2)x-Aryl-Hal are possible. According to the invention also Hal-(C(R1)2)xâZ-Aryl-Hal are possible.
Also in another embodiment of the invention halogenated hetaromates can be used. Some of these hetaromates are shown in FIG. 6. The hetaromates may contain in addition organic rests which do not react with the reactands of the process according to the invention.
Suitable nucleophilic groups for the reaction with the side chain halogenated polymers are shown in FIG. 7.
Hereby sulfinate groups SO2M are especially preferred. There the sulfinates react with the halogenes preferred by S-Alkylation, as depicted in FIG. 8 for the reaction of a side-chain halogenated polymer with lithium sulfinatophenylphosphonic acid dialkylester.
Surprisingly it has been found, that membranes with a proton conducting functional group at the end of an alkyl-, aryl- or alkylaryl side chain can be made according to the following process:
In a suitable solvent (see below), whereby dipolar-aprotic solvents are preferred, the following components are mixed:
If from the solution of these components a thin film is casted and then the solvent at increased temperature and if necessary reduced pressure is evaporated, covalently cross-linked membranes are formed, which contain the non-ionic form of the cation exchange group in the polymer side chain.
Suitable solvents for the reaction of the side-chain halogenated polymers with compounds containing a nucleophilic group and the ionic group or their non-ionic precursor are ether solvents as described above, hydrocarbon solvents (aliphatic or aromatic, as described above), dipolar-aprotic solvents such as NMP, DMAc, DMF, DMSO, Sulfolan, protic solvents such as alcoholes CnH2n+1, water or any other mixtures of these solvents with each other.
The reaction temperature for the metal organic reaction is from â100° C. to +100° C. Preferred is the temperature range from â80 to 0° C.
The reaction temperature for the reaction of the deprotonated polymer with the organic compound containing a halogen atom and one or more ionic groups or their non-ionic precursors is from â100° C. to +100° C. Preferred is the temperature range from â80 to 0° C.
The reaction temperature for the reaction of the deprotonated polymer with the dihalogen compounds is from â100° C. to +100° C. Preferred is the temperature range from â80 to 0° C.
The reaction temperature for the reaction of the side-chain halogenated polymer with nucleophilic groups and ionic groups or their non-ionic precursors is from â100° C. to +200° C. Preferred is the temperature range from â80 to +150° C.
Suitable solvents for the Michaelis-Arbusov-reaction of the side-chain halogenated polymers are ether solvents as described above, hydrocarbon solvents (aliphatic or aromatic, as described above), dipolar-aprotic solvents such as NMP, DMAc, DMF, DMSO, Sulfolan, protic solvents such as alcoholes CnH2n+1, water or any other mixture of these solvents with each other. Preferred are dipolar-aprotic solvents, especially preferred is DMSO.
Suitable catalyst systems for the Michaelis-Arbusov-reaction are NiCl2 (with use of Triethylphosphite as phosphonation agent) or Pd(PPh3)4/triethylamine (with use of (EtO)2POH as phosphonation agent). Preferred is Pd(PPh3)4/triethylamine as catalyst system.
Possible is also the use of sodium dialkylphosphite in THF as phosphonation agent. Also other processes known from the literature for this reaction are possible.
The reaction temperature for the Michaelis-Arbusov-reaction of the side-chain halogenated polymer with nucleophilic groups and ionic groups or their non-ionic precursors is from â100° C. to +200° C. Preferred is the temperature range from 0 to +150° C.
Suitable conditions for hydrolysis of the proton-conducting groups are:
11.05 g PSU Udel P 1800 (0.025 mol) dried
1000 ml THF anhydrous
5 ml n-BuLi 10 N (0.05 mol)
24.51 g (0.1 mol) Diethyl-2-Bromethylphosphonate (M=245.06 g/mol, δ=1.348 g/cm3)â18.2 ml
The reaction flask is loaded with THF under inert gas. Subsequently, the dried polymer powder is added under stirring and vigorous flushing with Argon. After the polymer is dissolved, it is cooled down to â60° C., under vigorous flushing with Argon. Then the polymer solution is titrated with n-BuLi (14 ml 2.5N n-BuLi, drum), until a slight yellow/orange colour indicates that the polymer solution is water-free from now on.
Then within 10 min the 10N n-BuLi is syringed in.
The stirring is continued for 2 hours. Then the solution of diethylbromethylphosphonate is added into the reaction mixture as fast as possible. Subsequently, the reaction mixture is stirred for 6 h at â60° C. Then, 100 ml solution is removed from the reaction mixture, which is hydrolyzed in methanol (EA and NMR), the temperature is increased to â40° C./24 h, subsequently to â20° C. and 0° C., under respective hydrolysis of 100 ml solution. Methanol is used as precipitant.
The precipitated polymer is dried at 60° C. From the product, the following analyses are prepared: 1Hâ, 13C and 31P-NMR, elemental analysis.
Relating to phosphorus content 1.37 groups per repeat unit are bound.
Reaction of Dilithiated PSU with ClâCH2âPOCl2
The reaction flask is loaded with THF under inert gas. Subsequently, the dried polymer powder is added under stirring and vigorous flushing with Argon. After the polymer is dissolved, it is cooled down to â60° C., under vigorous flushing with Argon. Then the polymer solution is titrated with n-BuLi (14 ml 2.5N n-BuLi, drum), until a slight yellow/orange colour indicates that the polymer solution is water-free from now on. Then within 10 min the 10N n-BuLi is syringed in. The stirring is continued for 2 hours. Then the solution of Chlormethanphosphonsäuredichloride (2-fold excess) is added into the reaction mixture as fast as possible. The solution changes colour at once to black and in a few minutes back to yellow-orange. Subsequently, the reaction mixture is stirred for 6 h at â40° C., increases the temperature for 24 h to â20° C., then for 12 h to 0° C. The polymer is precipitated from the solution with 4 l demineralised water. The polymer soon forms a yellow cake in the upper THF layer, which is separated and digested with methanol for 12 h.
The thus purified polymer is dried at 60° C. From the product, the following analyses are prepared: 1Hâ, 13C and 31P-NMR, elemental analysis.
Relating to phosphorus content 0.31 groups per repeat unit are bound.
Because the reaction at â60° C. is very fast, cool after addition of butyl lithium to â80° C., keep 12 h at â80° C., then follow the instructions as above from â60° C. to room temperature.
Reaction of Dilithiated PSU with Dibromhexane
The reaction flask is loaded with THF under inert gas. Subsequently, the dried polymer powder is added under stirring and vigorous flushing with Argon. After the polymer is dissolved, it is cooled down to â60° C., under vigorous flushing with Argon. Then the polymer solution is titrated with n-BuLi (14 ml 2.5N n-BuLi, drum), until a slight yellow/orange colour indicates that the polymer solution is water-free from now on. Then within 10 min the 10N n-BuLi is syringed in. The stirring is continued for 2 hours. Then the solution of dibromhexane is added into the reaction mixture as fast as possible. Subsequently, the reaction mixture is stirred for 12 h at â20° C., the temperature is increased to 0° C. for 4 h. The solution is hydrolysed with 10 ml MeOH, precipitated in 2 l MeOH, digested in MeOH and washed on the filter twice.
The thus purified polymer is dried at 25° C. under vacuum.
Relating to bromine content 0.87 groups per repeat unit are bound.
Reaction of Dilithiated PSU with Dibrombutane
The reaction flask is loaded with THF under inert gas. Subsequently, the dried polymer powder is added under stirring and vigorous flushing with Argon. After the polymer is dissolved, it is cooled down to â60° C., under vigorous flushing with Argon. Then the polymer solution is titrated with n-BuLi (14 ml 2.5N n-BuLi, drum), until a slight yellow/orange colour indicates that the polymer solution is water-free from now on. Then within 10 min the 10N n-BuLi is syringed in. The stirring is continued for 2 hours. Then the solution of dibrombutane is added into the reaction mixture as fast as possible. Subsequently, the reaction mixture is stirred for 12 h at â20° C., the temperature is increased to 0° C. for 4 h. The solution is hydrolysed with 10 ml MeOH, precipitated in 2 l MeOH, digested in MeOH and washed on the filter twice.
The thus purified polymer is dried at 25° C. under vacuum.
Relating to bromine content 0.98 groups per repeat unit are bound.
Reaction of Dilithiated PSU with Dibromdodecane
The reaction flask is loaded with THF under inert gas. Subsequently, the dried polymer powder is added under stirring and vigorous flushing with Argon. After the polymer is dissolved, it is cooled down to â60° C., under vigorous flushing with Argon. Then the polymer solution is titrated with n-BuLi (14 ml 2.5N n-BuLi, drum), until a slight yellow/orange colour indicates that the polymer solution is water-free from now on. Then within 10 min the 10N n-BuLi is syringed in. The stirring is continued for 2 hours. Then the solution of dibromdodecane is added into the reaction mixture as fast as possible. Subsequently, the reaction mixture is stirred for 12 h at â20° C., the temperature is increased to 0° C. for 4 h. The solution is hydrolysed with 10 ml MeOH, precipitated in 2 l MeOH, digested in MeOH and washed on the filter twice.
The thus purified polymer is dried at 25° C. under vacuum.
Relating to bromine content 0.3 groups per repeat unit are bound.
Reaction of Dilithiated PSU with Diiodbutane
The reaction flask is loaded with THF under inert gas. Subsequently, the dried polymer powder is added under stirring and vigorous flushing with Argon. After the polymer is dissolved, it is cooled down to â60° C., under vigorous flushing with Argon. Then the polymer solution is titrated with n-BuLi (14 ml 2.5N n-BuLi, drum), until a slight yellow/orange colour indicates that the polymer solution is water-free from now on. Then within 10 min the 10N n-BuLi is syringed in. The stirring is continued for 2 hours. Then the solution of diiodbutane is added into the reaction mixture as fast as possible. Subsequently, the reaction mixture is stirred for 12 h at â20° C., the temperature is increased to 0° C. for 4 h. The solution is hydrolysed with 10 ml MeOH, precipitated in 2 l MeOH, digested in MeOH and washed on the filter twice.
The thus purified polymer is dried at 25° C. under vacuum.
Relating to iodine content 1.51 groups per repeat unit are bound.
Reaction of Dilithiated PSU with Diioddecane
Chemicals:
The reaction flask is loaded with THF under inert gas. Subsequently, the dried polymer powder is added under stirring and vigorous flushing with Argon. After the polymer is dissolved, it is cooled down to â60° C., under vigorous flushing with Argon. Then the polymer solution is titrated with n-BuLi (14 ml 2.5N n-BuLi, drum), until a slight yellow/orange colour indicates that the polymer solution is water-free from now on. Then within 10 min the 10N n-BuLi is syringed in. The stirring is continued for 2 hours. Then the solution of diioddecane is added into the reaction mixture as fast as possible. Subsequently, the reaction mixture is stirred for 12 h at â20° C., the temperature is increased to 0° C. for 4 h. The solution is hydrolysed with 10 ml MeOH, precipitated in 2 l MeOH, digested in MeOH and washed on the filter twice.
The thus purified polymer is dried at 25° C. under vacuum.
Relating to iodine content 0.56 groups per repeat unit are bound.
3 g PSU(SO2Li)2 (2 sulfinate groups per PSU repeating unit, sulfinate-IEC=3.4 meq SO2Li/g polymer) are dissolved in 17 g NMP. 2.7 mmol meta-LiO2S-benzolphosphonic acid dioctylester (obtained by lithiation of benzolphosphonic acid dioctylester under Argon in THF and subsequent reaction with SO2) and 0.4 mmol 1,4-Diiodbutan are added to the solution and let to homogenise. Then the polymer solution is casted on a support (glas plate or metal plate and/or cloth/vlies/mocroporous membrane). The solvent is evaporated in a ventilated or vacuum drying ovenat increased temperature of 50 to 140° C. Hereby the sulfinate-S-alkylation of the sulfinato-benzolphosphonic acid ester and the diiodbutane takes place and the membrane cross-links. After solvent evaporation the membrane is posttreated to saponificate the phosphonic acid ester with 48% HBr or concentrated HCl under reflux.
1. Polymeric ionomers and ionomer membranes, characterised in that they are composed of a non- or partly-fluorinated, partly or fully aromatic main chain and a non- or partly fluorinated side chain with ionic groups or their non-ionic precursor and if are necessary covalently cross-linked.
2. Polymeric ionomers and ionomer membranes according to claim 1, characterised in that they contain the following structure:
3. Polymeric ionomers and ionomer membranes according to claim 1, characterised in that as polymer main chain the following polymers are possible:
Polyolefines like Polyethylen, Polypropylen, Polyisobutylen, Polynorbornen, Polymethylpenten, Poly(1,4-isopren), Poly(3,4-isopren), Poly(1,4-butadien), Poly(1,2-butadien) and Block-, alternating or statistical copolymers of polydiene, polybutadiene and polyisoprene with styrole
styrol(co)polymere like polystyrole, poly(methylstyrole), poly(ι,β,β-trifluorstyrole), poly(pentafluorostyrole)
perfluorinated ionomeres like NafionÂŽ or the SO2Hal-precursor of NafionÂŽ (Hal=F, Cl, Br, I), DowÂŽ-Membrane, GoreSelectÂŽ-Membrane.
partly-fluorinated polymeres like polyvinylidenfluoride, polyvinylfluoride and their copolymeres with polyolefines or with arylmain chain polymers of FIG. 5 (see below) N-basic polymeres like polyvinylcarbazole, polyethylenimine, poly(2-vinylpyridine), poly(3-vinylpyridine), poly(4-vinylpyridine)
(Het)aryl main chain polymers containing the construction units of FIG. 5.
4. Polymeric ionomeres and ionomer membranes according to claim 1, characterised in that as polymer main chain the following polymers are preferred:
polyetherketones like polyetherketone PEK VictrexÂŽ, polyetheretherketone PEEK VictrexÂŽ, polyetheretherketoneketone PEEKK, polyetherketonetherketone-ketone PEKEKK UltrapekÂŽ
polyethersulfone like polysulfone UdelÂŽ, polyphenylsulfone Radel RÂŽ, polyetherethersulfone Radel AÂŽ, polyethersulfone PES VictrexÂŽ
poly(benz)imidazole like PBI CelazolÂŽ and other oligomers and polymers containing the (Benz)imidazole unit, whereby the (Benz)imidazole group can be in main chain or in the polymer side chain polyphenylenether like Poly(2,6-dimethyloxyphenylen), Poly(2,6-diphenyloxyphenylen)
polyphenylensulfide and copolymeres
poly(1,4-phenylene) or poly(1,3-phenylene), which are modified in the side chain if necessary with benzoyl-, naphtoyl- or o-phenyloxy-1,4-benzoylgroups, m-phenyloxy-1,4-benzoylgroup or p-phenyloxy-1,4-benzoylgroups.
poly(benzoxazole) and copolymers
poly(benzthiazole) and copolymers
poly(phtalazinone) and copolymers
polyanilin and copolymers
polythiazoles
polypyrroles
5. Process to produce polymeric ionomeres and ionomer membranes according to claim 1, characterised in that as reagents for the Arylpolymer-Deprotonation the following reagents are used:
n-Butyllithium, sec-Butyllithium, tert. Butyllithium, Methyllithium, Phenyllithium, Grignard reagents as phenylmagnesiumhalogenide and other Grignard reagents, lithiumdiisopropylamide, and other lithium amides, sodium naphtalide, potassium naphtalide, zinc organic compounds (âRieke metalsâ).
6. Process to produce polymeric ionomeres and ionomer membranes according to claim 1, characterised in that as solvents for the deprotonation reaction the following solvents are used:
ether solvents like THF, diethylether, glyme, diglyme, triglyme, dioxane and other ether solvents as well as hydrocarbon solvents CnF2n+2, cyclohexane, benzene, toluene, xylole and other CâHâ aromatic solvants and any other mixtures thereof and with ether solvents, wherein ether solvents are preferred and THF is especially preferred.
7. Process to produce polymeric ionomeres and ionomer membranes according to claim 1, characterised in that as compounds with nucleophilically substitutable halogene atoms and ionic groups compounds with the following structure are used:
Hal-C(R1)xâY,
wherein Y and R1 are defined in FIG. 2.
8. Process to produce polymeric ionomeres and ionomer membranes according to claim 7, characterised in that as compounds with nucleophilically substitutable halogene atoms and ionic groups compounds with the following structure are preferred: Hal-(CH2)xâY, wherein Y and R1 are defined in FIG. 2.
9. Process to produce polymeric ionomeres and ionomer membranes according to claim 7, characterised in that as halogen atoms iodine and bromine are preferred.
10. Process to produce polymeric ionomeres and ionomer membranes according to claim 2, characterised in that the following dihalogene compounds are used in the reaction with the deprotonated polymers:
Hal-(C(R1)2)x-Hal (Hal=F,Cl,Br,I; R1âH,F,CnH2n+1, Aryl)
Brâ(C(R1)2)xâI
Hal-(C(R1)2)x-Aryl-Hal
Hal-(C(R1)2)xâZ-Aryl-Hal, wherein Z is defined in FIG. 5.
11. Process to produce polymeric ionomeres and ionomer membranes according to claim 2, characterised in that the following nucleophilic compounds are used in the reaction with the side-chain halogenated polymers:
12. Process to produce polymeric ionomeres and ionomer membranes according to claims 2 and 11, characterised in that for the reaction with side-chain halogenated polymers, compounds with a sulfinate group are preferred as nucleophilic compounds, which react by S-Alkylation with the halogenated polymers.
13. Process to produce polymeric ionomeres and ionomer membranes according to claims 2 and 11, characterised in that as solvents for the reaction of the side-chain halogenated polymers with compounds containing a nucleophilic group and the ionic group or their non-ionic precursor are ether solvents as described above, hydrocarbon solvents (aliphatic or aromatic, as described above), dipolar-aprotic solvents such as NMP, DMAc, DMF, DMSO, Sulfolan, protic solvents such as alcoholes CnH2n+1, water or any other mixtures of these solvents with each other are used.