CATION EXCHANGE POLYMERS AND ANION EXCHANGE POLYMERS AND CORRESPONDING (BLEND) MEMBRANES MADE OF POLYMERS CONTAINING HIGHLY FLUORINATED AROMATIC GROUPS, BY WAY OF NUCLEOPHILIC SUBSTITUTION
20230014901 · 2023-01-19
Inventors
Cpc classification
H01M8/1027
ELECTRICITY
H01M8/1039
ELECTRICITY
H01M8/188
ELECTRICITY
Y02E60/50
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
H01M8/1032
ELECTRICITY
H01M8/1044
ELECTRICITY
H01M8/1081
ELECTRICITY
H01M8/227
ELECTRICITY
B01J41/14
PERFORMING OPERATIONS; TRANSPORTING
B01D67/00931
PERFORMING OPERATIONS; TRANSPORTING
C08J9/28
CHEMISTRY; METALLURGY
C08J2325/18
CHEMISTRY; METALLURGY
C08F8/30
CHEMISTRY; METALLURGY
B01D71/82
PERFORMING OPERATIONS; TRANSPORTING
C08F8/30
CHEMISTRY; METALLURGY
H01M8/1023
ELECTRICITY
International classification
B01D67/00
PERFORMING OPERATIONS; TRANSPORTING
B01D71/82
PERFORMING OPERATIONS; TRANSPORTING
B01J41/14
PERFORMING OPERATIONS; TRANSPORTING
B01J47/12
PERFORMING OPERATIONS; TRANSPORTING
H01M8/1032
ELECTRICITY
H01M8/1039
ELECTRICITY
Abstract
The present invention relates to new anion exchange polymers and (blend) membranes made from polymers containing highly fluorinated aromatic groups by means of nucleophilic substitution and processes for their production by means of nucleophilic aromatic substitution and their areas of application in membrane processes, in particular in electrochemical membrane processes such as fuel cells, electrolysis and redox flow batteries.
Claims
1. Partially or perfluorinated low and high molecular weight aromatic compounds containing tertiary N-basic groups, characterized in that they can be obtained by means of (i) an aromatic nucleophilic substitution by reaction of one or more F of the partially or perfluorinated compound with a secondary N-base: a) ##STR00001## or (ii) an aromatic nucleophilic substitution by reaction of one or more F of the partially or perfluorinated compound with a secondary N-amide: ##STR00002##
3. Partially or perfluorinated low or high molecular weight aromatic compounds containing quaternized N-basic functional groups, characterized in that they are obtainable by quaternizing the compounds containing tertiary N-basic groups according to claim 1 with an alkylating agent: ##STR00003##
4. Partially or perfluorinated low or high molecular weight aromatic compounds containing quaternized N-basic functional groups, characterized in that they are obtainable by reaction of low or high molecular weight, partially or perfluorinated aromatic compounds with tertiary amines: ##STR00004##
5. Partially or perfluorinated low or high molecular weight aromatic compounds containing quaternized N-basic functional groups and other functional groups, characterized in that they are obtainable by nucleophilic substitution reaction with organic low or high molecular weight compounds containing secondary and/or tertiary N-basic groups or other organic low or high molecular weight compounds capable of nucleophilic substitution in the following ways: 1. Reaction of perfluoroarene with secondary N-amide and a second nucleophile, followed by quaternization: ##STR00005## 2. Reaction of perfluoroarene with secondary N-basic compound and a second nucleophile, followed by quaternization: ##STR00006## 3. Reaction of perfluoroarene with tertiary N-basic compound and a second nucleophile in one step (one-pot reaction): ##STR00007##
6. Compounds according to claim 1, characterized in that the organic compounds are high-molecular compounds with a molecular weight of between 1 kDa and 10,000 kDa.
7. Compounds according to claim 1, characterized in that the following polymers are used as partially or perfluorinated starting polymers: ##STR00008## ##STR00009## ##STR00010##
8. Compounds according to claim 1, characterized in that the following functional, tertiary and/or quaternary N-basic groups are used as the N-basic functional group introduced into the polymers: ##STR00011## ##STR00012##
9. Compounds according to claim 1, characterized in that, in addition to the N-basic compounds, the following compounds are used as further nucleophiles which can be introduced into the polymers by nucleophilic F exchange: ##STR00013## ##STR00014##
10. An ionically and/or covalently crosslinked blend membrane made from the oligomers or polymers according to claim 1, characterized in that the oligomers and/or polymers, dissolved separately in solvents, are mixed in any mixing ratio with the solutions of the following polymers: sulfonated and/or phosphonated and/or carboxylated polymers, basic polymers, where the basic polymers can have primary, secondary or tertiary N-basic groups in the side chain or the main chain, halomethylated polymers, where the halomethyl groups can function as covalent crosslinking groups.
11. A process for the production of blend membranes according to claim 10, characterized in that the blend components are dissolved separately in dipolar-aprotic solvents and/or ether solvents and/or protic (alcohol) solvents and then the solutions are mixed with one another in any mixing ratios, thereafter the mixture solutions are doctor knife coated, sprayed or printed on a substrate, the solvent (mixture) is evaporated in a vacuum oven or a convection oven at an elevated temperature of 30 to 180° C., then the membrane formed is detached from the substrate and optionally in various steps as follows is after-treated in order to activate it, whereby the order of the after-treatments is arbitrary and can contain all or just a part of the after-treatment liquids listed below: with deionized water at temperatures from 0 to 100° C., with a mineral acid solution of any concentration at temperatures from 0 to 130° C., with an alkali metal lye of any concentration at temperatures from 0 to 100° C., with any liquid tertiary N-base either in pure form or as a solution in water, in an alcohol and/or ether- and/or dipolar-protic solvents, in an aqueous or alcoholic metal salt solution of any concentration at temperatures from 0 to 100° C.
12. The process for the production of blend membranes according to claim 11, characterized in that the solvent for the blend components is a dipolar-aprotic solvent selected from dimethyl sulfoxide, dimethyl sulfone, diphenyl sulfone, sulfolane, N,N-dimethylacetamide, N,N-dimethylformamide, N-methylpyrrolidinone, formamide and dimethyl carbonate.
13. The process for the production of blend membranes according to claim 11, characterized in that the mineral acid is selected from sulfuric acid, phosphoric acid, or hydrochloric acid of any desired concentration for the post-treatment/doping of the blend membranes.
14. The ionically and/or covalently crosslinked blend membranes according to claim 10, characterized in that the following polymer types are used as blend components of the polymers from claim 1: as sulfonated, phosphonated or carboxylated polymers, polymers based on non-, partially- or perfluorinated vinyl hydrocarbon polymers, non-, partially- or perfluorinated polystyrenes or aryl main chain polymers including polyphenylenes, polyphenylene ethers, polyether sulfones, polyether ketones, polysulfones, polyketones, polyvinylcarbazoles, polyphenylenephosphine oxides, as basic polymers, polymers of the polyimidazole or polybenzimidazole type, where the imidazole group or benzimidazole group may be present in the main chain or the side chain of the polyimidazoles or polybenzimidazoles, as halomethylated polymers, chloro- or bromomethylated polymers including bromomethylated polyphenylene oxide, chloromethylated polyvinyl benzyl chloride or chloro- or bromomethylated polyphenylene.
15. An electrode ionomer comprising the polymers and blend membranes according to claim 1.
16. An electrode ionomer or an ionomer membrane comprising the blend membranes of claim 10.
17. The ionomer membrane of claim 10, wherein the ionomer membrane is incorporated in a fuel cell, electrolysis, a redox-flow battery, diffusion dialysis, electrodialysis, or a bipolar membrane with a cationic and anionic layer.
Description
[0005] The figures show:
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[0045] The first embodiment of the invention relates to the reaction of a perfluorinated aryl with a strong organic secondary or tertiary N-base, where the perfluorinated aryl may be a small molecule, an oligomer or a polymer. The first embodiment of the invention is shown in
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[0047]
[0048] The second embodiment of the invention relates to strong N-bases in which an NH bond is replaced by an N-alkali metal bond. These alkali metal-nitrogen compounds are alkali metal amides. The alkali metal can be Li, Na, K, Rb or Cs, with Li being preferred. The alkali metal amides react with the perfluorinated arene (low molecular weight, oligomer or polymer) with nucleophilic alkali metal-F-exchange (S.sub.N.sup.Ar), as shown in
[0049] In principle, any alkali metal amides can be reacted with the perfluoroarenes according to the invention. Lithium amides are preferred in the invention. A non-limiting selection of lithium amides is shown in
[0050]
[0051] A third embodiment of the invention relates to the substitution of additional F of the low molecular weight, oligomeric or high polymeric perfluoroarenes containing tertiary amino groups or quaternary ammonium groups by other nucleophiles. In principle, the type of nucleophile or nucleophiles substituting the F is not restricted, but all nucleophiles that react with perfluoroarenes with nucleophilic exchange of the F are suitable.
[0052] However, the following nucleophiles are preferred (without limiting the choice of nucleophiles): [0053] R—SH, [R—S].sup.−[C.sup.+] (R=any alkyl or aryl radical, C.sup.+=1-valent cation such as metal cation, ammonium ion, pyridinium ion, imidazolium ion, guanidinium ion, etc.). The nucleophile can also contain more than 1 SH or SC group. Non-limiting examples of R—SH are alkyl thiols C.sub.nH.sub.2n+1SH (n=2-20), non-limiting examples of RSC are alkyl or aryl or benzyl thiolates with alkali metal cation (alkali metal=Li, Na, K, Rb, Cs) or any ammonium ion as counterion. Non-limiting examples of compounds containing multiple SH or SC groups are benzenedithiols (ortho-, meta- or para-), naphthalenedithiol, dibenzyldithiols, alkanedithiols HS—C.sub.nH.sub.2n—SH (n=2-20) or their salts with metal or ammonium counterions with no limitation on the nature of the counter(cat)ion. [0054] P(OSi(CH.sub.3).sub.3).sub.3 (tris(trimethylsilyl)phosphite) [0055] AL.sub.2S and ALSH (AL=alkali metal counterion)
[0056] The third embodiment for obtaining the low molecular weight, oligomeric and polymeric compounds according to the invention can be obtained in the following sequence: [0057] (1) The low molecular weight, oligomeric or polymeric perfluoroarene is first reacted with the second nucleophile. If the second nucleophile is RSH or RSC, the resulting thioether bridge can then be oxidized to the sulfone bridge. If the nucleophile is AL.sub.2S or ALSH, the resulting SH group can be oxidized to the SO.sub.3H group. This is followed by reaction with the secondary or tertiary N-base or the secondary N-amide, followed by alkylation in the case of secondary N-bases or secondary N-amides. This reaction sequence is shown in
[0060] It was also found, surprisingly, that the novel polymers according to the invention in all of the above three embodiments can be readily converted with other suitable polymers to form blend membranes. A non-limiting selection of blend membranes according to the invention is listed below: [0061] Polymers of the 1st and 2nd embodiment (polymeric perfluorinated arenes with quaternary N-basic groups (see
[0067] The present invention is explained in more detail by the following examples without being restricted thereto.
1. Reaction of Poly (Pentafluorostyrene) with Tetramethylguanidine Followed by Alkylation of the Substituted Polymer with Dimethyl Sulfate
1.1 Synthesis Method of M-PPFSt-TMG
[0068] 1.1.1 Tetramethylguanidine-Modified PPFSt (PPFSt-TMG)
[0069] PPFSt (1 g, 5.15 mmol) was dispersed in DMAc (20 mL) at 130° C. for 2 h in a three-necked round bottom flask equipped with condenser, argon inlet and outlet. After cooling to room temperature, tetramethylguanidine (2.97 g, 25.8 mmol) was added into the reaction solution. The reaction solution was stirred at 130° C. for 24 hours. Then the polymer was precipitated by dropping the polymer solution into water. The polymer obtained was washed several times with plenty of water and dried in an oven at 60° C. for 24 hours. A degree of substitution of 100% was confirmed by 19F-NMR showing 2 peaks after the reaction (ortho and meta positions) (
[0070] 1.1.2 Quaternization of PPFSt-TMG (M-PPFSt-TMG)
[0071] Quaternization of PPFSt-TMG was performed by methylation using dimethyl sulfate. PPFSt-TMG (1 g, 3.45 mmol) was dissolved in 20 mL of DMAc in a round bottom flask equipped with septum, condenser, argon inlet and outlet for 3 hours at room temperature under an argon atmosphere. After complete dissolution, dimethyl sulfate (1 mL, 10.4 mmol) was slowly added via syringe. The reaction mixture was stirred at 90° C. for 16 hours. After cooling to room temperature, the polymer solution was precipitated in acetone. The polymer obtained was washed twice with acetone and oven dried at 60° C. for 24 hours. 100% DOS was confirmed by .sup.1H-NMR, showing a complete peak shift of the methyl groups (N—CH.sub.3 (a), from 2.5 ppm to 2.9 ppm), and a new peak can be identified by methylation (b) N—CH.sub.3 are assigned.
[0072] 1.1.3 Solubility tests of the synthesized polymers
TABLE-US-00001 TABLE 1 Solubility of the synthesized polymers in various solvents DMSO DMAc THF acetone methanol water chloroform PPFSt + + ++ ++ − − − PPFSt-TMG − ++ ++ ++ ++ − M-PPFSt- ++ ++ − − ++ ++ − TMG ++ soluble; + partially soluble; − insoluble
1.2 Synthesis of M-PPFSt-TBF-OX-TMG
[0073] Synthesis of PPFSt-TBF: PPFSt (1 g, 5.2 mmol) was dissolved in 40 mL of methyl ethyl ketone (MEK) in a 100 mL three-necked flask equipped with argon inlet, outlet, and condenser. After complete dissolution of PPFSt, triethylamine (7.82 g, 15 equivalents to PPFSt) and 4-fluorobenzenethiol (1.65 mL, 3 equivalents to PPFSt) were added to a polymer solution. Then the reaction mixture was kept at 75° C. for 24 hours. The synthesized polymer was obtained by precipitation in methanol. The polymer was washed several times with methanol and dried in an oven at 60° C. for 18 hours; almost complete substitution determined by .sup.19F NMR.
[0074] Synthesis of PPFSt-TBF-OX: PPFSt-TBF (3 g, 10 mmol) was dispersed in 60 mL of trifluoroacetic acid in a flask fitted with a condenser. Then 10 mL of hydrogen peroxide (30% in water, 100 mmol) was added dropwise to a reaction flask. A reaction solution was stirred at 30° C. for 72 hours, followed by 1 hour at 110° C. After cooling to room temperature, the reaction solution was poured into water to obtain the polymer. The polymer obtained was washed several times with water and dried in an oven at 60° C. for 18 hours; chemical shift of aromatic region indicates successful oxidation from sulfide to sulfone.
[0075] Synthesis of PPFSt-TBF-OX-TMG: PPFSt-TBF-OX (3.34 g, 10 mmol) was dissolved in DMAc in a three-necked flask equipped with argon inlet, outlet and condenser. After complete dissolution, TMG (10 mL, 80 mmol) was added into the polymer solution and stirred at 130° C. for 20 h. Then the polymer was isolated by precipitation in water. The polymer obtained was washed several times with water and dried in an oven at 60° C. for 24 hours; partial guanidization confirmed by .sup.1H-NMR: 3 peaks in the aromatic region and a strong peak at 2.6 ppm due to N—CH.sub.3 from tetramethylguanidine groups.
[0076] Synthesis of M-PPFSt-TBF-OX-TMG: Methylation of PPFSt-TBF-OX-TMG was performed with dimethyl sulfate (DMS) in DMAc. PPFSt-TBF-OX-TMG was dissolved in DMAc. After complete dissolution, DMS was added to a polymer reaction solution and the temperature was raised to 90° C. The reaction was mechanically stirred at this temperature for 20 hours. Then the polymer was obtained by precipitation in acetone. The polymer was washed with acetone and dried in an oven at 60° C. for 24 hours; chemical shift of a tetramethylguanidine peak from 2.6 to 3.7 ppm and a new peak at 3.4 ppm due to methylation.
2. Production of Blend Membranes from Reaction Product 4.1 and F.SUB.6.PBI
2.1 Blend Membrane Preparation
[0077] M-PPFSt-TMG polymer was dissolved in DMSO as a 5 wt % polymer solution. %. F.sub.6PBI was dissolved in DMSO at 80° C. as a 5 wt % solution. The two polymer solutions were mixed together in specific ratios as described in the table. A polymer blend solution was cast onto a glass plate and placed in a convection oven at 80° C. for 24 hours to evaporate the solvent. The resulting mixed membranes were peeled from the glass plate by immersion in deionized water. The mixed membranes were stored in a ziplock bag for further use. Mixed membranes of M-PPFSt-TBF-OX-TMG with F.sub.6PBI were prepared in the same way.
TABLE-US-00002 TABLE 2 Blend membrane preparation of M-PPFSt-TMG with F.sub.6PBI M-PPFSt-TMG/F.sub.6PBI membranes (w/w) observation M-PPFSt-TMG 80-20 80/20 too much swelling M-PPFSt-TMG 70-30 70/30 stretchy M-PPFSt-TMG 60-40 60/40 stretchy M-PPFSt-TMG 50-50 50/50 stretchy
TABLE-US-00003 TABLE 3 Blend membrane preparation of M-PPFSt-OX-TBF-TMG with F.sub.6PBI M-PPFSt-TMG/F.sub.6PBI membranes (w/w) observation M-PPFSt-TBF-OX-TMG 70-30 70/30 heterogeneous membrane M-PPFSt-TBF-OX-TMG 60-40 60/40 heterogeneous membrane M-PPFSt-TBF-OX-TMG 50-50 50/50 heterogeneous membrane
2.2 Blend Membrane Properties
[0078]
TABLE-US-00004 TABLE 4 Blend membrane properties IEC Conductivity in 1 M Conductivity in 1 M water absorption membrane (mmol/g) NaCl (mS/cm) H.sub.2SO.sub.4 (mS/cm) (%) M-PPFSt-TMG 80-20 2.46 61.7 — — M-PPFSt-TMG 70-30 2.47 14.2 43 ± 7.8 21 ± 1.9 M-PPFSt-TMG 60-40 2.72 1.31 33 ± 4.0 17 ± 0.9 M-PPFSt-TMG 50-50 2.91 0.44 22 ± 4.6 17 ± 4.0 — omitted due to excessive swelling
2.3 Vanadium Redox Flow Battery Performance
[0079] 2.3.1 Coulombic Efficiency (CE), Voltage Efficiency (VE) and Energy Efficiency (EE)
[0080] The Coulombic Efficiency (CE) (a), Voltage Efficiency ( ) VE (b) and Energy Efficiency (EE) (c) of blend membranes and a Nafion 212 membrane are shown in
[0081] 2.3.2 Self-Discharge Test
[0082] The self-discharge test of mixed membranes and a Nafion 212 membrane can be found in
[0083] 2.3.3 Long Term Cycling Test
[0084] The results of the long-term cycling test of blend membranes and of a Nafion 212 membrane can be found in
3. Reaction of Poly (Pentafluorostyrene) with 1-(2-Dimethylaminoethyl)-5-Mercaptotetrazole Followed by Reaction with Tetramethylguanidine
3.1 Reaction of Poly(Pentafluorostyrene) with 1-(2-Dimethylaminoethyl)-5-Mercaptotetrazole
[0085] The grafting of 1-(2-dimethylaminoethyl)-5-mercaptotetrazole onto poly (pentafluorostyrene) was performed according to the literature (if published, degree of substitution: 30%). Tetramethylguanidine was introduced onto partially grafted PPFSt-MTZ. 1 g of partially substituted PPFSt-MTZ was dissolved in 20 ml of DMAc equipped with a condenser, argon inlet and argon outlet. After completely dissolving at 90° C. for 1 hour, tetramethylguanidine was added into the polymer solution and kept at 130° C. for 24 hours. The polymer solution was precipitated in water. The polymer obtained (PPFSt-MTZ-TMG) was washed several times with water and dried in an oven at 60° C. for 24 hours.
[0086] Methylation: Methylation was carried out with dimethyl sulfate at 90° C. However, at this temperature a precipitate was observed.
4. Crosslinked Membranes of Partially Modified PPFSt and 1,6-Hexanedithiol
4.1 Production of Crosslinked Membranes (XL-M-PPFSt-MTZ)
[0087] In a glass vial, 0.3 g M-PPFSt-MTZ (prepared according to the literature, if published, 41% DOS) was dissolved in 10 ml DMSO. After complete dissolution, triethylamine (0.27 g) and 1,6-hexanedithiol (0.19 g) are added to the polymer solution. After homogenization, the mixed solution was poured into a Petri dish. This is placed in a closed oven (or with Petri dish cover) at 60° C. to ensure a reaction time of 1 day, followed by 8 hours at 120° C. with vacuum to remove residual chemicals. As shown in figure (b), a mechanically stable crosslinked membrane was obtained. The IEC of XL-M-PPFSt-MTZ was 0.28 mmol/g and the conductivity measured in 1 M H.sub.2SO.sub.4 was 1.77±0.18 mS/cm. Even the IEC and conductivity were lower compared to mixed membranes. Crosslinking using dithiol compounds is a possible fabrication route to obtain the mechanically stable membranes since the homo-M-PPFSt-MTZ polymer membrane was mechanically unstable.
5. Reaction of Poly (Pentafluorostyrene) with 1-Hexanethiol Followed by Reaction with Tetramethylguanidine
5.1 Reaction of Poly (Pentafluorostyren) with 1-Hexanethiol
[0088] In a 500 mL 3-necked round bottom flask equipped with a reflux condenser and an argon inlet and outlet, PPFSt (10 g, 51.5 mmol) was dissolved in THF (200 mL) at 90° C. for 1 hour under argon flow. The 1-hexanethiol (3.8 mL, 27.1 mmol) and DBU (8 mL, 52.5 mmol) were added at this temperature and stirred for 15 hours. After cooling to room temperature, the viscous solution was slowly poured into isopropanol to form a yellowish precipitate. The resulting polymer was washed several times with isopropanol and dried in a forced air oven at 60° C. for 24 hours.
[0089] Yield: 9.8 g
[0090] .sup.19F NMR (400 MHz, CDCl3, ppm): −134 (s, 2.8F), −143 (s, 4.9F), −154 (s, 1F). −161(s, 2.1F) (
[0091] .sup.1H NMR (400 MHz, CDCl3, ppm): 0.90 (t, 1.8H), 1.27-1.54 (m, ca. 5H), 1.99 (s, 2H), 2.41 (s, 0.8H), 2.88 (s, 1.2H))(
5.2 Reaction Between Product from 4.5.1 (PPFSt-TH) with Tetramethylguanidine
[0092] PPFSt-TH (8 g, 31.6 mmol) was dissolved in DMAc (200 mL) in a 500 mL 3-neck flask with condenser and argon flow at 130° C. for 2 hours. After cooling to room temperature, TMG (19.8 ml, 158 mmol) was dropped into the polymer solution and reacted at 130° C. for 24 hours. After cooling, the brownish reaction solution was precipitated dropwise in deionized water to obtain the polymer. The polymer was isolated by filtration and washed several times with deionized water. The final polymer was dried in a forced air oven at 60° C. for 24 hours.
[0093] Yield: 9.04 g
[0094]
5.3 Methylation Reaction Between Product from 4.5.2 (PPFSt-TH-TMG) and Dimethyl Sulfate (DMS)
[0095] PPFSt-TH-TMG (7 g, 24 mmol) was dissolved in DMAc (150 mL). After complete dissolution, DMS (20.5 mL, 72.1 mmol) was added to the reaction solution with a syringe. The reaction was maintained at 90° C. for 12 hours with vigorous stirring. The reaction solution was then added dropwise to diethyl ether and washed twice with diethyl ether and once with deionized water. The resulting polymer was dried in a vacuum oven at 60° C. under 1 mbar for 24 hours.
[0096] Yield: 7.5 g
[0097]
5.4 Membrane Manufacture
[0098] An m-PBI was dissolved at 5.2% by weight in DMAc. The m-PBI solution was cast onto a glass plate and the solvent evaporated in a forced air oven at 80° C. for 24 hours. The membrane was then peeled off the glass plate by soaking in a water bath. The resulting membrane was dried at 90° C. for 12 hours and stored in a ziplock bag before use. A 5 wt % polymer solution of
[0099] M-PPFSt-TH-TMG was prepared by dissolving in DMAc. The solution was poured onto a Teflon sheet and placed in a forced air oven at 60° C. for 24 hours to evaporate the solvent. The membrane was removed from the glass support by immersion in water. The resulting membrane was conditioned by 10 wt % aqueous sodium chloride solution at 60° C. for 3 days, followed by 1 day immersion in DI water at 60° C., washed extensively with DI water and then stored in a zip-lock bag before further use (
5.5 PA Doping of the Membranes
[0100] The PA doping was carried out by determining the weight before and after doping in aqueous PA solutions of different concentrations. Before PA doping, the membranes were dried at 6° C. for 24 hours, followed by measurement of their dry masses. The dried membrane samples were immersed in PA solutions at room temperature for 24 hours. The membrane samples were removed from the PA solution and blotted with a paper towel to remove phosphoric acid on the surfaces. Then the doped membranes were weighed (
Doping level (%)=[(W.sub.after−W.sub.dry)/W.sub.dry]×100
[0101] W.sub.after: membrane weight after PA doping, W.sub.dry: membrane weight before PA doping
Acid doping level (ADL) PA/functional group=[(W.sub.after−W.sub.dry)×0.85/97.99]/[(W.sub.dry/IEC of the membrane)×1000]
[0102] W.sub.after: Membrane weight after PA doping
[0103] W.sub.dry: Membrane dry weight
[0104] IEC: Ion Exchange Capacity
[0105] The degree of substitution was calculated from the integral ratios between substituted and unsubstituted aromatic rings in NMR spectra. The theoretical ion exchange capacity (CEC) of membranes was calculated from the function of the IEC with the degree of substitution (obtained from NMR).
5.6 Thermal Stability (TGA)
[0106] To investigate the thermal stability of the synthesized polymers, a thermogravimetric analysis (TGA) was performed using a NETZSCH TGA, model STA 499C, coupled to FT-IR; accomplished. The temperature was raised at a heating rate of 20° C. per minute under mixed oxygen and nitrogen atmosphere (oxygen: 56 mL/min, nitrogen: 24 mL/min). (
5.7 FT-IR Spectra
[0107] For the structural analysis of polymers, FTIR spectra were recorded at room temperature as a function of the wavenumber range from 4000 to 400 cm.sup.−1 with 64 scans and the attenuated total reflection (ATR) mode using a Nicolet iS5 FTIR spectrometer (
5.8 Fuel Cell Test
[0108] To fabricate a membrane-electrode assembly (MEA), a phosphoric acid-doped membrane was sandwiched between two electrodes. The gas diffusion electrode (GDE) was provided by Freudenberg and contained 1.5 mg Pt/cm.sup.2 and the same electrodes were used on both the anode and cathode sides with an active area of 23.04 cm.sup.2. The MEA was installed in a commercially available single cell, which had been sealed with a torque of 3 Nm. Fuel cell tests were performed using a commercial test station (Scribner 850e, Scribner Associates Inc.). Fuel cell performance was studied with non-humidified gases on both the anode and cathode sides at ambient pressure. The flow rates of H.sub.2 at the anode and air at the cathode were 0.25 and 1.25 L/min, respectively (