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  • H01M8/102—Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer
  • H01M8/1023—Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer having only carbon, e.g. polyarylenes, polystyrenes or polybutadiene-styrenes
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  • H01M8/1025—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
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  • H01M8/102—Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer
  • H01M8/1027—Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer having carbon, oxygen and other atoms, e.g. sulfonated polyethersulfones [S-PES]
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  • H01M8/1018—Polymeric electrolyte materials
  • H01M8/102—Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer
  • H01M8/103—Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer having nitrogen, e.g. sulfonated polybenzimidazoles [S-PBI], polybenzimidazoles with phosphoric acid, sulfonated polyamides [S-PA] or sulfonated polyphosphazenes [S-PPh]
• • H—ELECTRICITY
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  • H01M8/1018—Polymeric electrolyte materials
  • H01M8/102—Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer
  • H01M8/1032—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]
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  • H01M8/1072—Polymeric electrolyte materials characterised by the manufacturing processes by chemical reactions, e.g. insitu polymerisation or insitu crosslinking
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  • C08J2365/00—Characterised by the use of macromolecular compounds obtained by reactions forming a carbon-to-carbon link in the main chain; Derivatives of such polymers
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  • C08J2381/00—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
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  • Y02P70/50—Manufacturing or production processes characterised by the final manufactured product

Definitions

• Ionomermembranen consisting of a non- or partially fluorinated non-, partially or fully aromatic main chain and a non- or partially fluorinated side chain with ionogenic groups or their nonionic precursors
• Phosphoric or phosphonic acid-containing ionomer membranes have received increasing attention in recent years because the phosphoric or phosphonic acid groups exhibit anhydrous proton conductivity because phosphorous or phosphonic acid groups can function both as a proton donor and as a proton acceptor.
• This anhydrous proton conductivity of phosphoric acids is particularly interesting in fuel cells in the temperature range between 100 0 C and 200 ° C, since in this temperature range in fuel cells only a very low water vapor is present, and thus sulfonic acid ionomer membranes no longer work, since they rely on water molecules as proton acceptor are. From the literature various types of membranes are known whose proton conductivity is generated by phosphoric or phosphonic acids. For example:
• PBI Polybenzimidazole
• phosphoric acid blend membranes containing 5-6 phosphoric acid molecules per PBI repeating unit 1 , 2 . These membranes work very well at T> 100 ° C in the fuel cell, but at T ⁇ 100 ° C, the phosphoric acid can be discharged from the membrane, which leads to conductivity reduction and corrosion problems.
• Phosphonated poly phosphazenes
• brominated poly bisphenoxyphosphazene
• chlorophosphorus diphenyl ester reaction with chlorophosphorus diphenyl ester and subsequent partial hydrolysis of the resulting phosphonic acid diphenyl ester to the free phosphonic acid 3 .
• the object of the invention is to provide ionomers and ionomer membranes in which the ionogenic group sits on a flexible side chain, which has a positive effect on the ionic conductivity of the ionomers.
• the object is also to provide methods to access these polymeric Hf ⁇ -Leitern.
• the ionomers according to the invention are shown in FIG.
• ionomers and ionomer membranes with the ionogenic groups or their nonionogenic precursors can be synthesized at the end of a flexible side chain according to the following method 1 in the following stages:
• the base polymer is deprotonated by means of organometallic reaction
• Ib the deprotonated polymer is reacted with an aliphatic halogen compound which preferably carries the halogen atom at one end and a nonionic precursor of the ionic group at the other end, whereby the halogen is nucleophilicly exchanged;
• Ic the nonionic form of the ionic group is hydrolyzed, releasing the H + -FoHn of the cation exchange moiety.
• a method 2 also leads to ionomers and ionomer membranes having the H.sup. -Conducting group in the side chain: 2a: the base polymer is deprotonated by means of an organometallic reaction; 2b: the deprotonated polymer is reacted excessively with an aliphatic dihalogen compound or a mixture of different dihalogen compounds (different halogens and / or different chain lengths of the dihalogen compound (s) are possible), which preferably carries the halogen atoms at the ends of the molecule a part of the halogen atoms of the dihalo compound (s) is nucleophilicly exchanged: Ar-Li + Hal - ((C (R 2 ) 2 ) X- Hal -> Ar - ((C (R 2 ) 2 ) X- Hal 2c: the In the side chain nucleophil exchangeable halogen-containing polymers are reacted with a compound
• side-chain halogenated polymers can be converted into polymers with the phosphonic acid group in the side chain by Michaelis-Arbusov reaction or related reactions and subsequent hydrolysis. This reaction is shown schematically in Fig. 4.
• Polyolefms such as polyethylene, polypropylene, polyisobutylene, polynorbornene,
• Styrene (co) polymers such as polystyrene, poly (methylstyrene), poly ( ⁇ , ⁇ , ⁇ -trifluorostyrene),
• N-basic polymers such as polyvinylcarbazole, polyethyleneimine, poly (2-vinylpyridine),
• aryl main chain polymers such as:
• Polyether ketones such as polyether ketone PEK Victrex®, polyether ether ketone PEEK Victrex®, polyether ether ketone ketone PEEKK, polyether ketone ether ketone PEKEKK Ultrapek®
• Polyethersulfones such as Polysulfone Udel®, Polyphenylsulfone Radel R®, Polyetherethersulfone Radel A®, Polyethersulfone PES Victrex® Poly (benz) imidazoles such as PBI Celazol® and others the (benz) imidazole
• (Benz) imidazole group may be present in the main chain or in the polymer side chain
• Polyphenylene ethers such. Poly (2,6-dimethyloxyphenylene), poly (2,6-diphenyloxyphenylene)
• 1,4-benzoyl groups or p-phenyloxy-l, 4-benzoyl groups may be modified.
• Suitable reagents for the aryl polymer deprotonation are n-butyllithium, sec-butyllithium, tert. Butyllithium, methyllithium, phenyllithium, Grignard compounds such as phenylmagnesium halide and other Grignard compounds, lithium diisopropylamide, and other lithium amides, sodium naphtalide, potassium naphtalide, zinc organic compounds ("Rieke metals”)
• Suitable solvents for the organometallic reaction are ether solvents such as THF, diethyl ether, glyme, diglyme, triglyme, dioxane and other ethereal solvents as well as hydrocarbon solvents C n H 2n +! , Cyclohexane, benzene, toluene, xylene and other CH aromatics and any mixtures thereof and with ether solvents.
• ether solvents such as THF, diethyl ether, glyme, diglyme, triglyme, dioxane and other ethereal solvents as well as hydrocarbon solvents C n H 2n +! , Cyclohexane, benzene, toluene, xylene and other CH aromatics and any mixtures thereof and with ether solvents.
• the compounds having nucleophilically substitutable halogen atoms and ionogenic groups may contain, as halogen, F, Cl, Br, or I. In this case, Cl, Br, and I are preferred. It is also possible to use mixtures of organic compounds with different halogens and different alkyl chain lengths.
• dihaloalkanes can also be mixed dihaloalkanes, ie compounds of the type Br- (C (RO 2 VI), where the two halogen atoms have different reactivity to ensure that no crosslinking occurs in the reaction of Method 2. If for example, if the compound I- (CH 2 ) X- C1 is reacted with lithiated PSU, it is preferable to exchange the nucleophile I. It is preferable to use Cl, Br, and I.
• halogenated heteroaromatics can be used. Some of these heteroaromatics are shown in Fig. 6.
• the heteroaromatics may additionally contain organic radicals which do not react with the reactants of the process according to the invention.
• Sulfinate groups SO 2 M are particularly preferred.
• the sulfinates react with the halogens preferably under S-alkylation, as shown in Fig. 8 for the reaction of a side-chain halogenated polymer with Lithiumulfonatophenylphosphonkladialkylester.
• the membranes, at the end of an alkyl, aryl or Alkylarylchargeoli have a H + type functional group can also be prepared by the following method: hi a suitable solvent (see below) 5 while a dipolar-aprotic solvent preferably , the following components are mixed together: (1) a polymer containing at least sulfato groups SO 2 M;
• Suitable solvents for the reaction of the side chain halogenated polymers with the compounds containing a nucleophilic group and the ionogenic moieties or their nonionic precursors are ethereal solvents. as listed above, hydrocarbon solvents (aliphatic or aromatic, as listed above), dipolar aprotic solvents such as NMP, DMAc, DMF, DMSO, sulfolane, protic solvents such as alcohols C n H 2n + 1 , water or any mixtures of the listed solvents with one another.
• the reaction temperatures for the organometallic reactions are in the range -100 ° C to + 100 ° C. Preference is given to a temperature range of -80 to 0 ° C.
• reaction temperatures for the reaction of the deprotonated polymer with a halogen atom, and one or more ionic groups or their non-ionic precursors containing organic compound are in the range -100 0 C to +100 0 C. Preferred is a temperature range of -80 to 0 ° C. ,
• reaction temperatures for the reactions of the deprotonated polymer with the dihalo compounds are in the range -100 ° C to +100 0 C. Preferred is a temperature range of -80 to 0 ° C.
• reaction temperatures for the reaction of the side chain halogenated polymer with nucleophilic moieties and ionogenic moieties or their nonionic precursors containing compounds are in the range -100 ° C to + 200 ° C. Preference is given to a temperature range of -80 to + 150 ° C.
• Suitable solvents for the Michaelis-Arbusov reaction of the side chain halogenated polymers are ethereal solvents as listed above, hydrocarbon solvents (aliphatic or aromatic as listed above), dipolar aprotic solvents such as NMP, DMAc, DMF, DMSO, sulfolane, protic solvents such as alcohols C "H 2n + i, water or any mixtures of the listed solvents with one another. Preference is given here to dipolar aprotic solvents, particularly preferably DMSO.
• Suitable catalyst systems for the Michaelis-Arbusov reaction are NiCl 2 (using triethylphosphite as a phosphonating agent) or Pd (PPh 3 ) 4 / triethylamine (using (EtO) 2 POH as the phosphonating agent). In this case, Pd (PPh 3 ) 4 / triethylamine is preferred as the catalyst system. Also possible is the use of sodium dialkyl phosphite in THF as a phosphonating agent. Other literature known methods are possible.
• reaction temperatures for the Michaelis-Arbusov reaction of the sokettenhalogen seeking polymers are in the range -100 ° C to + 200 ° C. Preference is given to a temperature range of 0 to 15O 0 C.
• Suitable hydrolysis conditions for the hydrolysis of the nonionic precursors of the proton-conducting groups are:
• the THF is poured into the reaction vessel under protective gas. Thereafter, the dried polymer is added to the reaction vessel with stirring and vigorous purging with argon. After the polymer has dissolved, it is cooled down to -60 ° C under a strong stream of argon. Now titrate the polymer solution with n-BuLi (14 ml of 2.5 N n-BuLi, barrel) until a slight yellow / orange color indicates that the reaction mixture is now anhydrous. Thereafter, the IO N n-BuLi is injected within 10 minutes. You leave 2h stir long. Thereafter, the solution of diethylbromethylphosphonate is added to the reaction solution as quickly as possible.
• the THF is poured into the reaction vessel under protective gas. Thereafter, the dried polymer is added to the reaction vessel with stirring and vigorous purging with argon. After the polymer has dissolved, it is cooled down to -60 ° C under a strong stream of argon. Now titrate the polymer solution with n-BuLi (14 ml of 2.5 N n-BuLi, barrel) until a slight yellow / orange color indicates that the reaction mixture is now anhydrous. Thereafter, the 10 N n-BuLi is injected within 10 min. Leave to stir for 2 hours. Thereafter, the solution of chloromethanephosphonic dichloride (2-fold excess) is added to the reaction solution as quickly as possible.
• the solution suddenly turns black and turns yellow-orange within a few minutes. Thereafter, the reaction mixture is stirred for 6 h at -4O 0 C, the temperature is increased to - 20 0 C / 24 h, then to 0 0 CJIl h.
• the polymer solution is precipitated in 41% distilled water. The polymer forms after a short phase in the upper THF layer of a yellowish cake, which is skimmed off and digested with methanol for 12 h.
• the thus purified polymer is dried at 60 ° C.
• the following analyzes are performed on the product: 1 H, 13 C, and 31 P NMR, elemental analysis.
• the THF is poured into the reaction vessel under protective gas. Thereafter, the dried polymer is added to the reaction vessel with stirring and vigorous purging with argon. After the polymer has dissolved, it is cooled down to -60 ° C under a strong stream of argon. Now titrate the polymer solution with 2.5 N n-BuLi until a slight yellow / orange color indicates that the reaction mixture is now anhydrous. Thereafter, the IO N n-BuLi is injected within 10 minutes. Leave to stir for 2 hours. Then add the dibromohexane to the reaction solution as fast as possible. Thereafter, the reaction mixture is stirred for 12 h at -20 ° C, the temperature is raised to 0 ° C / 4 h. It is hydrolyzed with 10 ml MeOH, precipitated in 2 1 MeOH, digested in MeOH and washed again on the frit 2 times.
• the thus purified polymer is dried at 25 0 C in a vacuum.
• the THF is poured into the reaction vessel under protective gas. Thereafter, the dried polymer is added to the reaction vessel with stirring and vigorous purging with argon. After the polymer has dissolved, it is cooled down to -60 ° C under a strong stream of argon. Now titrate the polymer solution with 2.5 N n-BuLi until a slight yellow / orange color indicates that the reaction mixture is now anhydrous. Thereafter, the 10 N n-BuLi is injected within 10 min. Leave to stir for 2 hours. Then add the dibromobutane to the reaction solution as quickly as possible. Thereafter, the reaction mixture is stirred for 12 h at -20 ° C, the temperature is raised to 0 ° C / 4 h. It is hydrolyzed with 10 ml MeOH, precipitated in 2 1 MeOH, digested in MeOH and washed again on the frit 2 times.
• the thus purified polymer is dried at 25 0 C in a vacuum.
• the THF is poured into the reaction vessel under protective gas. Thereafter, the dried polymer is added to the reaction vessel with stirring and vigorous purging with argon. After the polymer is dissolved, it is cooled down to -60 0 C, under vigorous stream of argon. Now titrate the polymer solution with 2.5 N n-BuLi until a slight yellow / orange color indicates that the reaction mixture is now anhydrous. Thereafter, the 10 N n-BuLi is injected within 10 min. Leave to stir for 2 hours. Then add the dibromodecane as fast as possible to the reaction solution. Thereafter, the reaction mixture is stirred for 12 h at -20 ° C, the temperature is raised to 0 ° C / 4 h. It is hydrolyzed with 10 ml MeOH, precipitated in 2 1 MeOH 5 digested in MeOH and washed again on the frit 2 times.
• the thus purified polymer is dried at 25 ° C in a vacuum.
• the THF is poured into the reaction vessel under protective gas. Thereafter, the dried polymer is added to the reaction vessel with stirring and vigorous purging with argon. After the polymer is dissolved, it is cooled down to -60 0 C, under vigorous stream of argon. Now titrate the polymer solution with 2.5 N n-BuLi until a slight yellow / orange color indicates that the reaction mixture is now anhydrous. Thereafter, the IO N n-BuLi is injected within 10 minutes. Leave to stir for 2 hours. Then add the diiodobutane to the reaction solution as fast as possible. Thereafter, the reaction mixture is stirred for 12 h at -20 ° C, the temperature is raised to 0 0 C / 4 h. It is hydrolyzed with 10 ml MeOH, precipitated in 2 1 MeOH 5 digested in MeOH and washed again on the frit 2 times.
• the thus purified polymer is dried at 25 0 C in a vacuum. Based on the iodine content, 1.51 groups per formula unit are attached!
• the THF is poured into the reaction vessel under protective gas. Thereafter, the dried polymer is added to the reaction vessel with stirring and vigorous purging with argon. After the polymer has dissolved, it is cooled down to -60 ° C under a strong stream of argon. Now titrate the polymer solution with 2.5 N n-BuLi until a slight yellow / orange color indicates that the reaction mixture is now anhydrous. Thereafter, the IO N n-BuLi is injected within 10 minutes. Leave to stir for 2 hours. Then add the diiododecane to the reaction solution as soon as possible. Thereafter, the reaction mixture is stirred for 12 h at -20 ° C, the temperature is raised to 0 0 C / 4 h. It is hydrolyzed with 10 ml MeOH, precipitated in 2 1 MeOH, digested in MeOH and washed again on the frit 2 times.
• the thus purified polymer is dried at 25 0 C in a vacuum.

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• 2005
  • 2005-08-20 WO PCT/DE2005/001504 patent/WO2006018020A2/de active Application Filing
  • 2005-08-20 DE DE112005002051T patent/DE112005002051A5/de not_active Withdrawn
  • 2005-08-20 US US11/573,982 patent/US20100063168A1/en not_active Abandoned
  • 2005-08-20 EP EP05778891A patent/EP1786544A2/de not_active Withdrawn
  • 2005-08-20 JP JP2007526201A patent/JP2008510845A/ja active Pending
• 2011
  • 2011-12-19 US US13/330,614 patent/US8742021B2/en not_active Expired - Fee Related
• 2012
  • 2012-06-14 JP JP2012135259A patent/JP5766655B2/ja not_active Expired - Fee Related
• 2014
  • 2014-04-22 JP JP2014088619A patent/JP2014221896A/ja active Pending
  • 2014-11-12 US US14/293,904 patent/US9403162B2/en not_active Expired - Fee Related

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