WO2019131932A1 - ポリフェニレン化合物 - Google Patents
ポリフェニレン化合物 Download PDFInfo
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- WO2019131932A1 WO2019131932A1 PCT/JP2018/048300 JP2018048300W WO2019131932A1 WO 2019131932 A1 WO2019131932 A1 WO 2019131932A1 JP 2018048300 W JP2018048300 W JP 2018048300W WO 2019131932 A1 WO2019131932 A1 WO 2019131932A1
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- 0 C*c1cc(-c2c(C)ccc(*C)c2)c(C)cc1 Chemical compound C*c1cc(-c2c(C)ccc(*C)c2)c(C)cc1 0.000 description 3
- QPODZJWHQBEVNV-UHFFFAOYSA-N C#Cc(cc12)ccc1-c1ccccc1C21c2cc(C#C)ccc2-c2ccccc12 Chemical compound C#Cc(cc12)ccc1-c1ccccc1C21c2cc(C#C)ccc2-c2ccccc12 QPODZJWHQBEVNV-UHFFFAOYSA-N 0.000 description 1
- UXSGWHMCFNVVSE-UHFFFAOYSA-N CC1C(C2(C(C)(C3C=C4)C=C4Br)c4cc(Br)ccc4-c4ccccc24)=C3C=CC1 Chemical compound CC1C(C2(C(C)(C3C=C4)C=C4Br)c4cc(Br)ccc4-c4ccccc24)=C3C=CC1 UXSGWHMCFNVVSE-UHFFFAOYSA-N 0.000 description 1
- DNKCQHALLWRWOX-UHFFFAOYSA-N C[Si](C)(C)C#Cc(cc1C23c4cc(C#C[Si](C)(C)C)ccc4-c4ccccc24)ccc1-c1c3cccc1 Chemical compound C[Si](C)(C)C#Cc(cc1C23c4cc(C#C[Si](C)(C)C)ccc4-c4ccccc24)ccc1-c1c3cccc1 DNKCQHALLWRWOX-UHFFFAOYSA-N 0.000 description 1
- LTLHVKFHNHGSNE-UHFFFAOYSA-N FC(c(cc1)ccc1-c1cccc(-c2ccc(C(F)(F)F)cc2)c1)(F)F Chemical compound FC(c(cc1)ccc1-c1cccc(-c2ccc(C(F)(F)F)cc2)c1)(F)F LTLHVKFHNHGSNE-UHFFFAOYSA-N 0.000 description 1
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- 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
- C08J5/2206—Films, membranes or diaphragms based on organic and/or inorganic macromolecular compounds
- C08J5/2218—Synthetic macromolecular compounds
- C08J5/2256—Synthetic macromolecular compounds based on macromolecular compounds obtained by reactions other than those involving carbon-to-carbon bonds, e.g. obtained by polycondensation
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- C08G61/00—Macromolecular compounds obtained by reactions forming a carbon-to-carbon link in the main chain of the macromolecule
- C08G61/02—Macromolecular compounds containing only carbon atoms in the main chain of the macromolecule, e.g. polyxylylenes
- C08G61/10—Macromolecular compounds containing only carbon atoms in the main chain of the macromolecule, e.g. polyxylylenes only aromatic carbon atoms, e.g. polyphenylenes
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- H—ELECTRICITY
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- H01B—CABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
- H01B1/00—Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors
- H01B1/06—Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors mainly consisting of other non-metallic substances
- H01B1/12—Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors mainly consisting of other non-metallic substances organic substances
- H01B1/124—Intrinsically conductive polymers
- H01B1/128—Intrinsically conductive polymers comprising six-membered aromatic rings in the main chain, e.g. polyanilines, polyphenylenes
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- H01M8/10—Fuel cells with solid electrolytes
- H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
- H01M8/1018—Polymeric electrolyte materials
- H01M8/102—Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer
- H01M8/1023—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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- H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
- H01M8/1018—Polymeric electrolyte materials
- H01M8/1069—Polymeric electrolyte materials characterised by the manufacturing processes
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- C08G2261/10—Definition of the polymer structure
- C08G2261/13—Morphological aspects
- C08G2261/133—Rod-like building block
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- C08G2261/30—Monomer units or repeat units incorporating structural elements in the main chain
- C08G2261/31—Monomer units or repeat units incorporating structural elements in the main chain incorporating aromatic structural elements in the main chain
- C08G2261/312—Non-condensed aromatic systems, e.g. benzene
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- H01M2300/0082—Organic polymers
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- Y—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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
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Definitions
- the present invention relates to a polyphenylene compound and a fuel cell using the same.
- a solid polymer fuel cell has an anode catalyst layer, a cathode catalyst layer, and a solid electrolyte membrane sandwiched between both catalyst layers.
- the electrolyte used for the solid electrolyte membrane is required to have proton conductivity, gas barrier property, electronic insulation and durability.
- Fluorine-based ionomers are used as electrolytes satisfying such characteristics.
- fluorine-based ionomers have been considered as alternative materials because of their high cost and environmental impact.
- the anode catalyst layer and the cathode catalyst layer also contain an electrolyte.
- this electrolyte the same material as the solid electrolyte membrane may be used in some cases, but the electrolyte of the catalyst layer is required to have gas permeability and electron conductivity in addition to proton conductivity.
- hydrocarbon-based ionomers having an aromatic skeleton as a skeleton and having a sulfone group introduced into the skeleton are used as electrolytes for a solid electrolyte membrane and a catalyst layer as a substitute material for a fluorine-based ionomer. It is disclosed.
- An object of the present invention is to provide a non-halogen containing compound which is excellent in proton conductivity and can be suitably used for a solid polymer fuel cell.
- A is a structure represented by the following general formula (II) or (III)
- B is a structure represented by the following general formula (VII)
- Each structural unit is randomly copolymerized, And, at least one benzene ring in the formula (I) has at least one sulfo group.
- R 1 to R 4 are each independently selected from hydrogen and an alkyl group having 1 to 3 carbon atoms, or R 1 and R 2 are together) Form an aromatic ring or fused aromatic ring and R 3 and R 4 together form an aromatic ring or fused aromatic ring, or R 1 , R 3 , R 4 is hydrogen and R 2 is a single A bond which is bonded to the carbon of c,
- X is a single bond or a structure represented by the following formula (IV), the following formula (V) or the following formula (VI),
- bond a is both bonded at the ortho position or both at the meta position with respect to the carbon bonded to X
- X is a group of the following formula (IV)
- the bond a is a structure represented by the following formula (V)
- the bond a is both bonded to the carbon bonded to X at the para position
- the bond a is For carbon attached to X, both are attached at the para position
- the structure represented by A is The compound according to [1], which is at least one selected from the group consisting of [3] The compound of [1] or [2] for a fuel cell. [4] The compound of [3], which is used as an electrolyte of an anode catalyst layer and / or a cathode catalyst layer of a fuel cell. [5] A catalyst layer of a fuel cell containing the compound of any one of [1] to [4].
- a compound represented by the following formula (VIII), a compound represented by the following formula (IX), and a compound represented by any of the following formula (X) are reacted to give a table of the following formula (XI)
- Obtaining a compound to be (In the above general formulas (IX) and (XI), l, n, A and B are as defined in the formula (I), provided that each benzene ring does not have a sulfo group) And 2.
- the compounds of the present invention exhibit excellent proton conductivity when used in the catalyst layer of a solid polymer fuel cell.
- the present invention relates to a compound having a structure represented by the following general formula (I).
- A is a structure represented by the following general formula (II) or (III)
- B is a structure represented by the following general formula (VII)
- Each structural unit is randomly copolymerized,
- at least one benzene ring in the formula (I) has at least one sulfo group.
- R 1 to R 4 are each independently selected from hydrogen and an alkyl group having 1 to 3 carbon atoms, or R 1 and R 2 are together) Form an aromatic ring or fused aromatic ring and R 3 and R 4 together form an aromatic ring or fused aromatic ring, or R 1 , R 3 , R 4 is hydrogen and R 2 is a single A bond which is bonded to the carbon of c,
- X is a single bond or a structure represented by the following formula (IV), the following formula (V) or the following formula (VI),
- bond a is both bonded at the ortho position or both at the meta position with respect to the carbon bonded to X
- X is a group of the following formula (IV)
- the bond a is a structure represented by the following formula (V)
- the bond a is both bonded to the carbon bonded to X at the para position
- the bond a is For carbon attached to X, both are attached at the para position
- alkyl group having 1 to 3 carbon atoms which is an option of R 1 to R 4 include a methyl group, an ethyl group, an n-propyl group and an i-propyl group. Of these, methyl is preferred.
- Such a structure is adopted because the polyphenylene structure is bulky and A is preferably twisted with respect to the main chain, whereby the gas permeability is excellent and the sulfo group is By having it, it is considered that it is possible to exhibit flexibility by being excellent in proton conductivity and further by having an arbitrary phenylene structure.
- R 1 to R 4 each independently represent hydrogen or an alkyl group having 1 to 3 carbon atoms
- X is a single bond
- a bond a is As an example of bonding to ortho carbons or to both carbons to which carbons are bonded together, Can be mentioned.
- R 1 to R 4 each independently represent hydrogen or an alkyl group having 1 to 3 carbon atoms
- X is represented by formula (IV)
- a bond a is For carbon bound to X, as an example attached to para position together: Can be mentioned.
- R 1 and R 2 together form an aromatic ring or a fused aromatic ring
- R 3 and R 4 together form an aromatic ring or a fused aromatic ring
- X As an example in which is a single bond, and the bond a is both bonded at the ortho position or both at the meta position with respect to the carbon bonded to X, Can be mentioned.
- R 1 and R 2 together form an aromatic ring or a fused aromatic ring
- R 3 and R 4 together form an aromatic ring or a fused aromatic ring
- X is As an example of a single bond in which the bond a is both attached at the ortho position to the carbon bonded to X, Can be mentioned.
- R 1 to R 4 each independently represent hydrogen or an alkyl group having 1 to 3 carbon atoms
- X is represented by the formula (V)
- a bond a is
- carbon bound to X as an example bound to the para position together: Can be mentioned.
- R 1 , R 3 and R 4 are hydrogen, and R 2 is a single bond and is bonded to carbon of c, and X is represented by formula (V), As an example in which the bond a is both attached at the meta position to the carbon attached to X, Can be mentioned.
- R 1 , R 3 and R 4 are hydrogen, and R 2 is a single bond and is bonded to the carbon of c, X is represented by the formula (VI), and the formula In (II), there is only one bond a, and A is bonded to another structure or structural unit by one bond a and bond b as an example, Can be mentioned.
- a in the formula (I) is At least one selected from the group consisting of Among them, at least one structure selected from the following group is more preferable, The following structure is more preferred.
- each structural unit which is mole fraction l and n is copolymerized at random. Specifically, as apparent from the manufacturing method described later, A and B are not adjacent to each other.
- At least one benzene ring in the compound represented by the formula (I) has at least one sulfo group.
- the benzene ring also includes the benzene ring contained in A and B.
- the sulfo group is preferably present at least on the benzene ring of the side chain in the compound represented by the formula (I).
- the number of sulfo groups per total benzene ring forming the side chain and the main chain is preferably 1 to 11, more preferably 2 to 6, and still more preferably 4.
- the weight average molecular weight (Mw) measured by the method described in the examples of the compound represented by formula (I) is preferably 1 ⁇ 10 3 to 1 ⁇ 10 6, more preferably 5 ⁇ 10 3 to 5 ⁇ 10 5 And 1 ⁇ 10 4 to 2 ⁇ 10 5 are more preferable.
- the proton exchange capacity (IEC) of the compound represented by the formula (I) is preferably 0.5 to 5.0 meq / g, more preferably 0.8 to 3.0 meq / g, and 0.9 to 2.0 meq / G is more preferable. Incidentally, this value is a value measured by the method described in the example.
- Process 1 In the step 1, the compound represented by the formula (VIII), the compound represented by the formula (IX), and the compound represented by any formula (X) are subjected to the Diels-Alder reaction to obtain the formula (VIII) And the triple bond of the compound represented by the formula (IX) and any compound represented by the formula (X) react to form a six-membered ring, The carbonyl group of the compound represented by the formula (VIII) is eliminated, and the irreversible reaction proceeds to obtain the compound represented by the formula (XI).
- the reaction temperature is usually 100 to 300 ° C.
- the compound represented by the formula (IX) and the compound represented by the formula (X) are prepared, for example, by reacting a halogenated starting material with ethynyltrimethylsilane and removing the trimethylsilane group. It can be obtained by releasing.
- a sulfo group is introduced into one or more benzene rings in the formula (XI).
- the reagent to be reacted with the formula (XI) include trimethylsilyl chloride sulfate, chlorosulfonic acid, fuming sulfuric acid, sulfuric acid and the like, and these reagents have a unit structure calculated using the mole fraction in the formula (XI)
- the reaction is preferably carried out in an equivalent ratio of 0.5 to 6 times the molecular weight per unit.
- the reaction temperature is usually 0 to 100 ° C.
- the sulfo group may be introduced into any benzene ring in the formula (XI) including the benzene ring contained in A and B.
- the compound of the formula (I) include the following compounds. (In the formula, l and n are as defined in the formula (I), and 0 ⁇ x ⁇ 14.)
- Step 1 a sulfo group is introduced into one or more benzene rings in formula (VIII).
- the reagent to be reacted with the formula (VIII) includes trimethylsilyl chloride sulfate, chlorosulfonic acid, fuming sulfuric acid, sulfuric acid and the like, and these reagents have a unit structure calculated using the molar fraction in the formula (XI)
- the reaction is preferably carried out in an equivalent ratio of 0.5 to 6 times the molecular weight per unit.
- the reaction temperature is usually 0 to 100 ° C.
- the sulfo group may be introduced into any benzene ring in the formula (VIII) including the benzene ring contained in A and B, and the number of sulfo groups is not particularly limited.
- the following compound (XII) Can be mentioned.
- step 2 the sulfo group in the compound of formula (VIII) introduced in step 1 is used as an amine salt.
- the reagent to be reacted with the compound of the formula (VIII) into which a sulfo group has been introduced includes triethylamine.
- the reaction temperature is not particularly limited and proceeds at room temperature.
- step 3 the compound of the formula (VIII) obtained in the step 2, in which at least one sulfo group converted into an amine salt is introduced, the compound represented by the formula (IX) and an arbitrary formula (X) Diels-Alder is reacted with a compound represented by the above to obtain a compound represented by the formula (I).
- the progress of the reaction is the same as described in the production method of (A).
- the reaction temperature is usually 100 to 300 ° C.
- the number of sulfo groups introduced can be controlled.
- FIG. 1 is a cross-sectional view schematically showing the structure of a fuel cell.
- the fuel cell 100 includes an anode catalyst layer 103, a cathode catalyst layer 105, and a solid electrolyte film 107 sandwiched between the two catalyst layers, and each catalyst layer is also referred to as a gas diffusion layer (hereinafter referred to as "GDL"). ) 101).
- GDL gas diffusion layer
- MEA membrane electrode assembly
- the membrane electrode assembly (MEA) is usually sandwiched by the separator 109.
- the compound represented by the formula (I) can be used for the anode catalyst layer 103, the cathode catalyst layer 105, and the solid electrolyte film 107 of the fuel cell, and used for the anode catalyst layer 103 and the cathode catalyst layer 105 of the fuel cell. It is more preferable to use at least the cathode catalyst layer 105 from the viewpoint of suppression of an overvoltage rise due to a decrease in oxygen gas diffusivity during high current driving.
- the catalyst layers 103 and 105 each include a catalyst component, a catalyst carrier for supporting the catalyst component, and an electrolyte.
- a known catalyst can be used without particular limitation as a catalyst component in the anode catalyst layer 103, and a known catalyst can be used without particular limitation as a catalyst component in the cathode catalyst layer 105.
- Examples of catalyst components used for the anode catalyst layer 103 and the cathode catalyst layer 105 include platinum, gold, silver, ruthenium, iridium, rhodium, palladium, osmium, tungsten, lead, iron, chromium, cobalt, nickel, and the like.
- Examples thereof include metals such as manganese, vanadium, molybdenum, gallium and aluminum, and alloys thereof.
- Examples of the catalyst support include carbon particles such as carbon black, activated carbon, coke, natural graphite, artificial graphite and the like.
- an electrolyte the compound represented by said Formula (I) is used.
- the catalyst layers 103 and 105 include the catalyst component, a catalyst carrier for supporting the catalyst component, and an electrolyte, and a method of applying a composition in which they are dispersed in a dispersion medium on a solid electrolyte membrane or a gas diffusion layer
- a composition comprising the catalyst component, a catalyst carrier for supporting the catalyst component, and an electrolyte, and a composition in which they are dispersed in a dispersion medium is coated on a substrate and dried to form a catalyst layer, and then the catalyst layer Can be produced by a known production method such as a method of transferring to a solid electrolyte.
- the compound represented by the above formula (I) can coat the catalyst supported on the catalyst carrier with a suitable thickness, so that it has good gas diffusivity and proton conductivity while maintaining the function of the catalyst. is there.
- the amount of the compound represented by the above formula (I) to the catalyst is preferably 0.1 to 10 times.
- Materials for the solid electrolyte film 107 include Nafion (registered trademark, manufactured by DuPont Co., Ltd.), Aquivion (registered trademark, manufactured by Solvay Corporation), Flemion (registered trademark, manufactured by Asahi Glass Co., Ltd.), Aciplex (registered trademark, Asahi Kasei Co., Ltd.) Perfluorosulfonic acid polymers such as those manufactured by the company, and from the viewpoint of proton conductivity, compounds represented by the above-mentioned formula (I) can be mentioned.
- the porous material which has electroconductivity is used suitably, for example, a carbon paper and nonwoven fabric, a felt, a nonwoven fabric etc. are mentioned as such a material.
- GPC gel permeation chromatography
- a membrane obtained by the method described later is 42 ⁇ 42 mm, and using this membrane and GTR Tech GTR-10XF, the temperature is set to 80 ° C., and the membrane both-side humidity is set to 90% RH, oxygen The permeability was measured.
- the measurement method was in accordance with Japanese Industrial Standard JIS K 7126-2 (GC).
- Synthesis Example 1 Synthesis of Compound M-1 In a reaction vessel under a nitrogen atmosphere, 5.16 g of 2,2 '-(1,4-phenylene) bis (1-phenylene-1,2-dione) and 6.66 g of 1,3-diphenylpropan-2-one, respectively. Then, 320 ml of ethanol was added. The reaction solution was heated to reflux, then a solution prepared with 1.69 g of potassium hydroxide and 8 ml of ethanol was added dropwise, and the mixture was stirred for 30 minutes under heating reflux condition. The mixture was allowed to cool to room temperature, stirred for 1 hour while cooling with an ice bath, and filtered. The obtained filtrate was dried to obtain 8.94 g (yield: 86%) of the target M-1.
- Synthesis Example 2 Synthesis of Compound M-2 In a reaction vessel under a nitrogen atmosphere, 3.00 g of 4,4 ′ ′-dibromo-1,1 ′: 3 ′, 1 ′ ′-terphenyl, 0.22 g of PdCl 2 (PPh 3 ) 2 and 0.030 g of copper iodide Then, 0.17 g of triphenylphosphine, 30 ml of diisopropylamine, and 1.64 g of ethynyltrimethylsilane were added, and the mixture was stirred for 3 hours under heating and reflux conditions. After cooling the reaction solution to room temperature, methanol was added and filtration was performed.
- the filtrate was collected and dissolved by adding 65 ml of methylene chloride, and a solution prepared by dissolving 1.53 g of sodium hydroxide in 30 ml of methanol was added and stirred at room temperature. After 15 minutes, ion-exchanged water was added to the reaction liquid and the phases were separated, and the organic phase was washed with saturated brine and then filtered through silica gel. The solvent of the filtrate was distilled off under reduced pressure, and the residue was dried to obtain 1.61 g (yield 75%) of the objective M-2.
- Synthesis Example 3 Synthesis of Compound M-3 (1) Synthesis of M-3 TMS In a reaction vessel under a nitrogen atmosphere, 2.00 g of 2,2'-dibromo-9,9'-spirobi [fluorene], 0.12 g of PdCl 2 (PPh 3 ) 2 , and iodide 0.016 g of copper, 0.089 g of triphenylphosphine, 20 ml of diisopropylamine, and 0.90 g of ethynyltrimethylsilane were added and stirred for 3 hours under heating and reflux conditions. The reaction solution was filtered and the filtrate obtained was concentrated and dried. Chloroform was added to the concentrated residue for dissolution, and separation and purification were performed by column chromatography to obtain 1.10 g (yield 51%) of the target M-3 TMS.
- Synthesis Example 4 Synthesis of Compound M-4 (1) M-4 TMS Under nitrogen atmosphere, the reaction vessel 2,7-dibromo-9,9'-spirobi 3.00g of [fluorene], PdCl 2 (PPh 3) 2 0.18g, copper iodide 0.024 g, 0.13 g of triphenylphosphine, 30 ml of diisopropylamine, and 1.44 g of ethynyltrimethylsilane were added and stirred for 6 hours under heating and reflux conditions. After methanol was added to the reaction solution, the filtrate obtained by filtration was dried to obtain 2.69 g (yield 84%) of the target M-4 TMS.
- Example 1 Production of Sample 1 (1) Synthesis of BP-1 Under a nitrogen atmosphere, 2.48 g of M-1, 1.00 g of M-2 and 25 ml of nitrobenzene were charged in a reaction vessel and stirred at 190 ° C. for 24 hours. The reaction solution was added dropwise to 500 ml of ethyl acetate, stirred, and filtered. The filtrate was dried to obtain 3.13 g (yield 95%) of the desired BP-1. The obtained BP-1 was Mn 33000, Mw 95800, PD (Mw / Mn) 2.9.
- Example 3 Production of Sample 3 (1) Synthesis of BP-3 Under a nitrogen atmosphere, 0.57 g of M-1, 0.30 g of M-3 and 3 ml of nitrobenzene were added and stirred at 170 ° C. for 20 hours. After nitrobenzene was added to the reaction solution, it was dropped into methanol, stirred at room temperature, and filtered. The filtrate was dried to obtain 0.77 g (yield 91%) of the desired BP-3. Mn 20200, Mw 64700, PD 3.2
- Example 4 Production of Sample 4 (1) Synthesis of BP-4 In a nitrogen atmosphere, 0.60 g of M-1, 0.077 g of 1,4-diethynylbenzene, 0.095 g of M-3, and 3 ml of nitrobenzene were charged into a reaction vessel, and the mixture was stirred at 190 ° C. for 8 hours. The reaction solution was cooled to about 100 ° C., and after adding and stirring nitrobenzene, this solution was dropped into methanol and stirred at room temperature. After filtration, the resulting filtrate was dried to obtain 0.69 g (yield 92%) of the desired BP-4. Mn 26000, Mw 77000, PD 3.0
- Example 5 Production of Sample 5 (1) Synthesis of BP-5 Under a nitrogen atmosphere, 0.60 g of M-1, 0.088 g of 1,4-diethynylbenzene, 0.064 g of M-3, and 3 ml of nitrobenzene were charged into a reaction vessel and stirred at 190 ° C. for 24 hours. The reaction solution was cooled to about 100 ° C., toluene was added and stirred, and then the solution was dropped into methanol and stirred at room temperature. After filtration was performed, toluene was added to the obtained filtrate to obtain a solution, which was then dropped into methanol again, and stirring was performed at room temperature. After filtration, the resulting filtrate was dried to obtain 0.67 g (yield 95%) of the desired BP-5. Mn 44100, Mw 146000, PD 3.3
- Example 6 Production of Sample 6 (1) Synthesis of BP-5 BP-5 was synthesized in the same manner as (1) of Example 5.
- Example 7 Production of Sample 7 (1) Synthesis of M-5 Under a nitrogen atmosphere, 4.00 g of M-1 and 300 mL of dichloromethane were added to the reaction vessel, and then 8.76 g of trimethylsilylchlorosulfonate was dropped, and the mixture was stirred at room temperature for 18 hours. After the reaction was stopped by adding 5 mL of ethanol to the reaction solution, the reaction solution was dropped into diethyl ether and stirred at room temperature. After filtration, the filtrate was dried to obtain 4.27 g of the target M-5 (yield: 73%).
- Comparative Example 1 The compound of the following formula was manufactured as sample 7 according to the description of US Patent Publication No. 7,301,002.
- ⁇ Deposition method> The resulting samples 1, 6 and 7 were subjected to film formation by the following method. To 50 mg of the sample, 450 mg of N, N-dimethylacetamide was added and dissolved, and then 0.2 ⁇ m PTFE filter filtration was performed, and the solution was applied on a glass substrate. After evaporating the solvent on a hot plate at 60 ° C. for 2 hours, at 80 ° C. for 6 hours, and at 100 ° C. for 2 hours, drying is further carried out with a vacuum dryer at 80 ° C. for 6 hours. 7 free standing films were obtained. Table 2 shows the results of measurement of proton exchange capacity, proton conductivity and oxygen permeability of the free standing membranes obtained from Samples 1, 6 and 7.
- Reference Signs List 100 fuel cell 101 gas diffusion layer 103 anode catalyst layer 105 cathode catalyst layer 107 solid electrolyte film 109 separator
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Abstract
Description
固体電解質膜に用いられる電解質には、プロトン伝導性、ガスバリア性、電子絶縁性及び耐久性が求められる。このような特性を満たす電解質としてフッ素系アイオノマーが用いられている。しかしながら、フッ素系アイオノマーは、高コストで環境負荷もあるため、代替材料が検討されてきた。
特許文献1及び特許文献2には、フッ素系アイオノマーの代替材料として、芳香族を骨格に有し、骨格にスルホン基を導入した炭化水素系アイオノマーを固体電解質膜及び触媒層の電解質に用いることが開示されている。
本願発明は、プロトン伝導性に優れ、固体高分子燃料電池に好適に使用することのできる非ハロゲン含有化合物を提供することを目的とする。
[1]下記一般式(I)で表される構造を有する化合物。
(上記一般式(I)中、l、nは、l+n=1.0とした場合のモル分率であって、0≦l<1.0、0<n≦1.0であり、
Aは、下記一般式(II)、又は(III)で表される構造であり、
Bは、下記一般式(VII)で表される構造であり、
各構造単位は、ランダム共重合しており、
且つ、式(I)中の少なくとも一つのベンゼン環が少なくとも一つのスルホ基を有する。)
(上記一般式(II)または(III)において、R1~R4は、それぞれ独立に、水素及び炭素数1~3のアルキル基から選択されるか、R1とR2が一緒になって芳香環もしくは縮合芳香環を形成しかつR3とR4が一緒になって芳香環もしくは縮合芳香環を形成しているか、又はR1、R3、R4が水素でありかつR2は単結合であってcの炭素と結合しており、
Xは、単結合、又は下記式(IV)、下記式(V)若しくは下記式(VI)で表される構造であり、
Xが単結合であるとき、結合aは、Xに結合している炭素に対して、ともにオルト位置に結合しているか、又はともにメタ位置に結合しており、Xが、下記式(IV)で表される構造であるとき、結合aは、Xに結合している炭素に対してともにパラ位置に結合しており、下記式(V)で表される構造であるとき、結合aは、Xに結合している炭素に対して、ともにパラ位置に結合しているか、又はともにメタ位置に結合しており、
Xが下記式(VI)で表される構造であるとき、上記一般式(II)または(III)における結合aは一方のみであり、Aは、一方の結合aと結合bとによって、他の構造又は構造単位と結合している。)
[2]前記一般式(I)において、Aで表される構造が、
からなる群から選ばれる少なくとも1種である[1]の化合物。
[3]燃料電池用である[1]又は[2]の化合物。
[4]燃料電池のアノード触媒層及び/又はカソード触媒層の電解質として用いられる[3]の化合物。
[5][1]~[4]のいずれかの化合物を含む燃料電池の触媒層。
[6]下記式(VIII)で表される化合物と下記式(IX)で表される化合物と任意の下記式(X)で表される化合物とを反応させて、下記式(XI)で表される化合物を得る工程1と、
(上記一般式(IX)及び(XI)中、l、n、A及びBは式(I)と同義である。ただし、各ベンゼン環はスルホ基を有さない。)
前記式(XI)で表される化合物をスルホン化して、前記式(I)で表される化合物を得る工程2とを含む、[1]の化合物の製造方法。
[7]下記式(VIII)の化合物中にアミン塩となったスルホ基を少なくとも1つ有する化合物と下記式(IX)で表される化合物と任意の下記式(X)で表される化合物とを反応させて前記式(I)で表される化合物を得る工程を含む、[1]の化合物の製造方法。
(上記一般式(IX)中、Aは式(I)と同義である。)
(上記一般式(I)中、l、nは、l+n=1.0とした場合のモル分率であって、0≦l<1.0、0<n≦1.0であり、
Aは、下記一般式(II)、又は(III)で表される構造であり、
Bは、下記一般式(VII)で表される構造であり、
各構造単位は、ランダム共重合しており、
且つ、式(I)中の少なくとも一つのベンゼン環が少なくとも一つのスルホ基を有する。)
(上記一般式(II)または(III)において、R1~R4は、それぞれ独立に、水素及び炭素数1~3のアルキル基から選択されるか、R1とR2が一緒になって芳香環もしくは縮合芳香環を形成しかつR3とR4が一緒になって芳香環もしくは縮合芳香環を形成しているか、又はR1、R3、R4が水素でありかつR2は単結合であってcの炭素と結合しており、
Xは、単結合、又は下記式(IV)、下記式(V)若しくは下記式(VI)で表される構造であり、
Xが単結合であるとき、結合aは、Xに結合している炭素に対して、ともにオルト位置に結合しているか、又はともにメタ位置に結合しており、Xが、下記式(IV)で表される構造であるとき、結合aは、Xに結合している炭素に対してともにパラ位置に結合しており、下記式(V)で表される構造であるとき、結合aは、Xに結合している炭素に対して、ともにパラ位置に結合しているか、又はともにメタ位置に結合しており、
Xが下記式(VI)で表される構造であるとき、上記一般式(II)または(III)における結合aは一方のみであり、Aは、一方の結合aと結合bとによって、他の構造又は構造単位と結合している。)
一般式(II)または(III)において、R1~R4は、それぞれ独立に、水素又は炭素数1~3のアルキル基であって、Xが単結合であって、結合aが、Xに結合している炭素に対して、ともにオルト位置に結合しているか、ともにメタ位置に結合している例としては、
が挙げられる。
が挙げられる。
が挙げられる。
が挙げられる。
が挙げられる。
が挙げられる。
が挙げられる。
からなる群から選ばれる少なくとも1種が好ましく、
なかでも下記の群から選ばれる少なくとも1種の構造がより好ましく、
下記の構造がさらに好ましい。
なお、モル分率l及びnである各構造単位は、ランダムに共重合している。
具体的には、後述する製造方法から明らかなように、AとBとが隣接することはない。
(A)Diels-Alder反応の後にスルホ化を行なう製造方法
式(I)で表される化合物は、下記式(VIII)で表される化合物と下記式(IX)で表される化合物と任意の下記式(X)で表される化合物とを反応させて、下記式(XI)で表される化合物を得る工程1と、
(上記一般式(IX)及び(XI)中、l、n及びA、Bは式(I)と同義である。ただし、各ベンゼン環はスルホ基を有さない。)
前記式(XI)で表される化合物をスルホン化して、前記式(I)で表される化合物を得る工程2とを含む製造方法によって製造することができる。
工程1では、前記式(VIII)で表される化合物と前記式(IX)で表される化合物と任意の前記式(X)で表される化合物とがDiels-Alder反応によって前記式(VIII)で表される化合物の五員環と前記式(IX)で表される化合物及び任意の前記式(X)で表される化合物の三重結合とが反応して六員環を形成するとともに、前記式(VIII)で表される化合物のカルボニル基が脱離して、不可逆的な反応が進行し、式(XI)で表される化合物が得られる。
反応温度は、通常100~300℃である。
なお、前記式(IX)で表される化合物及び任意の前記式(X)で表される化合物は、例えばハロゲン化された出発物質を、エチニルトリメチルシランと反応させた後、トリメチルシラン基を脱離することにより得ることができる。
工程2では、式(XI)中の1つ以上のベンゼン環にスルホ基を導入する。
式(XI)と反応させる試薬としては、クロリド硫酸トリメチルシリル、塩化スルホン酸、発煙硫酸、硫酸等が挙げられ、これらの試薬は式(XI)中のモル分率を使用して算出される単位構造当たりの分子量に対して、当量比で0.5~6倍の量で反応させる事が好ましい。
反応温度は、通常0~100℃である。
スルホ基は、A、Bに含まれるベンゼン環も含めた式(XI)中のいずれのベンゼン環にも導入され得るが、たとえば、式(I)の化合物として以下の化合物が挙げられる。
(式中l、nは式(I)と同義、0<x≦14である。)
(1)工程1
工程1では、式(VIII)中の1つ以上のベンゼン環にスルホ基を導入する。
式(VIII)と反応させる試薬としては、クロリド硫酸トリメチルシリル、塩化スルホン酸、発煙硫酸、硫酸等が挙げられ、これらの試薬は式(XI)中のモル分率を使用して算出される単位構造当たりの分子量に対して、当量比で0.5~6倍の量で反応させる事が好ましい。
反応温度は、通常0~100℃である。
スルホ基は、A、Bに含まれるベンゼン環も含めた式(VIII)中のいずれのベンゼン環にも導入され得、またスルホ基の数も特に制限されないが、たとえば、以下の化合物(XII)が挙げられる。
工程2では、工程1で導入された式(VIII)の化合物におけるスルホ基をアミン塩とする。
スルホ基の導入された式(VIII)の化合物と反応させる試薬としては、トリエチルアミンが挙げられる。
反応温度は、特に制限はなく、室温で進行する。
工程3では、工程2で得られた、アミン塩となったスルホ基が少なくとも1つ導入されている式(VIII)の化合物と前記式(IX)で表される化合物と任意の前記式(X)で表される化合物とをDiels-Alder反応させて式(I)で表される化合物を得る。その反応の進行については、(A)の製造方法で述べたのと同様である。
反応温度は、通常100~300℃である。
製造方法(B)によれば、導入されるスルホ基の数を制御することができる。
図1は、燃料電池の構成を模式的に示す断面図である。
燃料電池100は、アノード触媒層103、カソード触媒層105及び両触媒層に挟持された固体電解質膜107を有し、各触媒層は外側にガス拡散層(Gas Diffusion Layer、以下「GDL」ともいう。)101を有する。この構成を膜電極接合体(Membrane Electrode Assembly、以下「MEA」ともいう)という。燃料電池は、通常、この膜電極接合体(MEA)がセパレータ109に挟持されている。
前記式(I)で表される化合物は、燃料電池のアノード触媒層103、カソード触媒層105及び固体電解質膜107に用いることができ、燃料電池のアノード触媒層103、カソード触媒層105に用いることが好ましく、高電流駆動時における酸素ガス拡散性の低下に起因する過電圧上昇抑制の観点から少なくともカソード触媒層105に用いることがより好ましい。
アノード触媒層103における触媒成分としては、特に制限なく公知の触媒を使用することができ、カソード触媒層105における触媒成分としては、特に制限なく公知の触媒を使用することができる。このようなアノード触媒層103及びカソード触媒層105に用いられる触媒成分としては、例えば、白金、金、銀、ルテニウム、イリジウム、ロジウム、パラジウム、オスミウム、タングステン、鉛、鉄、クロム、コバルト、ニッケル、マンガン、バナジウム、モリブデン、ガリウム、アルミニウム等の金属およびこれらの合金などが挙げられる。
触媒担体としては、例えばカーボンブラック、活性炭、コークス、天然黒鉛、人造黒鉛などの炭素粒子が挙げられる。
電解質としては、前記式(I)で表される化合物が用いられる。
(1)重量平均分子量及び数平均分子量
ゲルパーミエーションクロマトグラフィー(以下、GPCと略称する)による測定結果である。測定には東ソー(株)製GPC装置を用い、測定条件等は次のとおりである。
GPCカラム: TSKgel SuperHZM-N;TSKgel SuperHZ3000;TSKgel SuperHZ2000(東ソー(株))
カラム温度:40℃
溶媒: テトラヒドロフラン(THF)
流量:0.6ml/min
標準試料:ポリスチレン(東ソー(株))
後述した方法により得られる膜を、室温で24時間2M NaCl水溶液に浸漬し、その浸漬液を0.02M NaOH水溶液にて中和滴定した。中和に要した0.02M NaOH量と浸漬前の膜重量からプロトン交換容量を算出した。
Scribner社の膜抵抗測定システムMTS740を用いて、温度と加湿条件を80℃及び湿度60%に設定し、膜厚み方向でのイオン伝導度を測定し、それからプロトン伝導性を算出した。
後述した方法により得られる膜を42×42mmとし、この膜とGTRテック社製GTR-10XFを用いて、温度を80℃、膜両面湿度を90%RHに設定し、酸素透過度を測定した。測定方法は、日本工業規格JIS K7126-2(GC)に従った。
窒素雰囲気下、反応容器に2,2’-(1,4-フェニレン)ビス(1-フェニレン-1,2-ジオン)5.16g、1,3-ジフェニルプロパン-2-オン6.66gをそれぞれ入れ、エタノール320mlを加えた。反応液を加熱し、還流させた後、水酸化カリウム1.69gとエタノール8mlで調製した溶液を滴下し、加熱還流条件下30分撹拌した。室温まで放冷した後、氷浴で冷却しながら更に1時間撹拌した後、ろ過を行った。得られたろ物を乾燥し、目的とするM-1を8.94g(収率 86%)得た。
窒素雰囲気下、反応容器に4,4’’-ジブロモ-1,1’:3’,1’’-ターフェニル3.00g、PdCl2(PPh3)20.22g、ヨウ化銅0.030g、トリフェニルホスフィン0.17g、ジイソプロピルアミン30ml、及び、エチニルトリメチルシラン1.64gを入れ、加熱還流条件下3時間撹拌した。反応液を室温まで冷却した後、メタノールを加え、ろ過を行った。ろ物を集め、塩化メチレン65mlを加え溶解させた後、水酸化ナトリウム1.53gをメタノール30mlに溶解させて調製した溶液を加え、室温で撹拌した。15分後反応液にイオン交換水を加え分液し、有機相を飽和食塩水で洗浄した後、シリカゲルろ過を行った。ろ液の溶媒を減圧留去した後、乾燥を行い目的とするM-2を1.61g(収率75%)得た。
(1)M-3 TMSの合成
窒素雰囲気下、反応容器に2,2'-ジブロモ-9,9'-スピロビ[フルオレン]を2.00g、PdCl2(PPh3)20.12g、ヨウ化銅0.016g、トリフェニルホスフィン0.089g、ジイソプロピルアミン20ml、及び、エチニルトリメチルシラン0.90gを入れ、加熱還流条件下3時間撹拌した。反応液を濾過して得られたろ液を濃縮し、乾燥した。濃縮残渣にクロロホルムを加えて溶解させ、カラムクロマトにて分離、精製を行い目的とするM-3 TMSを1.10g(収率 51%)得た。
窒素雰囲気下、反応容器にM-3 TMS1.10g、炭酸カリウム2.11g、THF/ MeOH (1:1=v/v)の混合溶媒200mlを入れ、室温で2時間撹拌した。反応液に塩化メチレンとイオン交換水を加え分液した。得られた有機相を濃縮、乾燥し、カラムクロマトにより分離精製を行い、目的物M-3を0.56g(収率 70%)得た。
(1)M-4 TMSの合成
窒素雰囲気下、反応容器に2,7-ジブロモ-9,9'-スピロビ[フルオレン]を3.00g、PdCl2(PPh3)20.18g、ヨウ化銅0.024g、トリフェニルホスフィン0.13g、ジイソプロピルアミン30ml、及び、エチニルトリメチルシラン1.44gを入れ、加熱還流条件下6時間撹拌した。反応液にメタノールを加えた後、ろ過して得られたろ物を乾燥し目的とするM-4 TMSを2.69g(収率 84%)得た。
窒素雰囲気下、反応容器にM-4 TMS2.69g、及び、塩化メチレン30mlを加え溶解を確認した後、水酸化ナトリウム1.05gとメタノール20mlで調製した溶液を滴下し、室温で30分撹拌した。反応液にイオン交換水を加え分液し、有機相を飽和食塩水で洗浄した後、濃縮、乾燥を行い目的とするM-4を1.85g(収率 96%)得た。
(1)BP-1の合成
窒素雰囲気下、反応容器にM-1を2.48g、M-2を1.00g、及び、ニトロベンゼン25mlを入れ190℃で24時間撹拌した。反応液を酢酸エチル500ml中に滴下し、撹拌を行った後、ろ過を行い、ろ物を乾燥して目的とするBP-1を3.13g(収率 95%)得た。得られたBP-1は、Mn33000,Mw95800, PD (Mw/Mn) 2.9であった。
窒素雰囲気下、反応容器にBP-1を0.20g、塩化メチレン5mlを加え、室温下撹拌して溶解させた。溶解確認後トリメチルシランスルホニルクロリド0.083gと塩化メチレン0.5mlで調製した溶液を滴下し、室温で5時間半撹拌した。反応液にエタノールを加え、反応を停止させた後、反応液をアセトン中に滴下し、室温で撹拌した。ろ過を行った後、ろ物を乾燥して、目的とする試料1(上記化学式中Sample 1、以下同様)を0.18g得た。
プロトン交換容量(IEC) 1.16 meq/g
(1)BP-2の合成
窒素雰囲気下、M-1を3.24g、M-4を1.71g、ニトロベンゼンを35ml入れ、190℃で15時間撹拌した。反応液を酢酸エチルに滴下し、室温で撹拌した後、ろ過を行った。ろ物を乾燥し、目的とするBP-2を2.68g(収率 57%)で得た。
Mn16400,Mw40800,PD 2.5
窒素雰囲気下、反応容器にBP-2を0.20g、塩化メチレン5mlを加え、室温下撹拌して溶解させた。溶解確認後トリメチルシランスルホニルクロリド0.076gと塩化メチレン0.5mlで調製した溶液を滴下し、室温で3時間撹拌した。反応液にエタノールを加え、反応を停止させた後、反応液をメタノール中に滴下し、室温で撹拌した。ろ過を行い、ろ物を乾燥して、目的とする試料2を0.18g得た。
(1)BP-3の合成
窒素雰囲気下、M-1を0.57g、M-3を0.30g、ニトロベンゼンを3ml入れ、170℃で20時間撹拌した。反応液にニトロベンゼンを加えた後、メタノール中へ滴下し、室温で撹拌した後、ろ過を行った。ろ物を乾燥し、目的とするBP-3を0.77g(収率 91%)で得た。
Mn20200,Mw64700,PD 3.2
窒素雰囲気下、反応容器にBP-3を0.30g、塩化メチレン5mlを加え、室温下撹拌して溶解させた。溶解確認後トリメチルシランスルホニルクロリド0.11gと塩化メチレン0.5mlで調製した溶液を滴下し、室温で1時間撹拌した。反応液にエタノールを加え、反応を停止させた後、反応液をn-ヘキサン中に滴下し、室温で撹拌した。ろ過を行い、ろ物を乾燥して、目的とする試料3を0.26g得た。
(1)BP-4の合成
窒素雰囲気下、反応容器にM-1を0.60g、1,4-ジエチニルベンゼン0.077g、M-3を0.095g、及び、ニトロベンゼン3mlを入れ190℃で8時間撹拌した。反応液を100℃程度まで冷却し、ニトロベンゼンを加え撹拌した後、この溶液をメタノール中に滴下し、室温で撹拌した。ろ過を行い得られたろ物を乾燥し目的とするBP-4を0.69g(収率 92%)得た。
Mn26000,Mw77000,PD 3.0
窒素雰囲気下、反応容器にBP-4を0.30g、塩化メチレン5mlを加え、室温下撹拌して溶解させた。溶解確認後トリメチルシランスルホニルクロリド0.14gと塩化メチレン0.5mlで調製した溶液を滴下し、室温で1時間半撹拌した。反応液にエタノールを加え、反応を停止させた後、反応液をアセトン中に滴下し、室温で撹拌した。ろ過を行い、ろ物を乾燥して、目的とする試料4を0.26g得た。
(1)BP-5の合成
窒素雰囲気下、反応容器にM-1を0.60g、1,4-ジエチニルベンゼン0.088g、M-3を0.064g、及び、ニトロベンゼン3mlを入れ190℃で24時間撹拌した。反応液を100℃程度まで冷却し、トルエンを加え撹拌した後、この溶液をメタノール中に滴下し、室温で撹拌した。ろ過を行い得られたろ物にトルエンを加え溶液とした後、再度メタノール中に滴下し、室温で撹拌を行った。ろ過を行い、得られたろ物を乾燥し目的とするBP-5を0.67g(収率 95%)得た。
Mn44100,Mw146000,PD 3.3
窒素雰囲気下、反応容器にBP-5を0.30g、塩化メチレン7mlを加え、室温下撹拌して溶解させた。溶解確認後トリメチルシランスルホニルクロリド0.14gと塩化メチレン0.5mlで調製した溶液を滴下し、室温で30分撹拌した。反応液にエタノールを加え、反応を停止させた後、反応液をアセトン中に滴下し、室温で撹拌した。ろ過を行い、ろ物を乾燥して、目的とする試料5を0.28g得た。
プロトン交換容量(IEC) 0.93 meq/g
(1)BP-5の合成
実施例5の(1)と同様にしてBP-5を合成した。
窒素雰囲気下、反応容器にBP-5を0.15g、塩化メチレン3.5mlを加え、室温下撹拌して溶解させた。溶解確認後トリメチルシランスルホニルクロリド0.14gと塩化メチレン0.5mlで調製した溶液を滴下し、室温で2時間半撹拌した。反応液にエタノールを加え、反応を停止させた後、反応液をn-ヘキサン中に滴下し、室温で撹拌した。ろ過を行い、ろ物を乾燥して、目的とする試料 6を0.13g得た。
プロトン交換容量(IEC) 1.59 meq/g
(1)M-5の合成
窒素雰囲気下、反応容器にM-1を4.00gとジクロロメタン300mLを加えた後、トリメチルシリルクロロスルホネート8.76gを滴下し、室温で18時間撹拌した。反応液にエタノール5mLを加え、反応を停止させた後、反応液をジエチルエーテル中に滴下し、室温で撹拌した。ろ過を行い、ろ物を乾燥して、目的とするM-5を4.27g(収率:73%)得た。
1H NMR(500MHz,DMSO-d6)δ(ppm):6.86(s,4H),6.92(d,J=7.5Hz,4H),7.07(d,J=8.5Hz,4H),7.13(d,J=8.5Hz,4H),7.25(t,J=7.5Hz,4H),7.33(t,J=7.5Hz,2H),7.47(d,J=8.0Hz,4H),7.51(d,J=8.0Hz,4H).
反応容器にM-5を4.00g、n-ブタノール185mL、及び、トリエチルアミン91mLを加え、室温で20分撹拌した。反応液をろ過した後、ろ物を乾燥して目的とするM-6を5.2g(収率:93%)を得た。
1H NMR(500MHz,DMSO-d6)δ(ppm):1.17(t,J=7.5Hz,36H),3.09(q,J=7.5Hz,24H),6.87(s,4H),6.92(d,J=7.0Hz,4H),7.08(d,J=8.5Hz,4H),7.14(d,J=8.5Hz,4H),7.26(t,J=7.0Hz,4H),7.34(m,2H),7.48(m,4H),7.51(d,J=8.0Hz,4H).
窒素雰囲気下、反応容器にM-6を0.997g、1,4-ジエチニルベンゼン0.0706g、M-3を0.0513g、及び、ニトロベンゼン9ml入れ、180℃で16時間加熱撹拌した。反応容器内の不溶物を取り出し、DMFに溶解させた後、酢酸エチル中に滴下し再沈殿させた。ろ過を行い、得られたろ物を乾燥し、0.956gのポリマーを得た。このポリマーにメタノールを加えた懸濁液に、2M KOHメタノール溶液を75mL滴下し、室温で2時間撹拌した。その後、ろ過、乾燥を行い、0.859gのポリマーのカリウム塩を得た後、これにイオン交換水を加えて懸濁液を作成した。この懸濁液に対し、2M H2SO4水溶液を加え、室温で2時間撹拌した。ろ過を行い、得られたろ物を乾燥して目的とするスルホン酸ポリマーである試料7を0.293g(収率:59%)得た。
Mn38400,Mw48400,PD 1.3
得られた試料1、6及び7について、以下の方法で成膜を行なった。
試料50mgに対して、N,N-ジメチルアセトアミドを450mg加え、溶解させた後0.2μmのPTFE製フィルターろ過を行い、ガラス基板上に塗布した。ホットプレート上で60℃で2時間、80℃で6時間、100℃で2時間かけて溶媒を蒸発させた後、更に、80℃の真空乾燥機で6時間乾燥を行い、試料1、6及び7の自立膜を得た。
試料1、6、及び7から得られた自立膜について、プロトン交換容量、プロトン伝導度及び酸素透過性を測定した結果を表2に示す。
101 ガス拡散層
103 アノード触媒層
105 カソード触媒層
107 固体電解質膜
109 セパレータ
Claims (7)
- 下記一般式(I)で表される構造を有する化合物。
(上記一般式(I)中、l、nは、l+n=1.0とした場合のモル分率であって、0≦l<1.0、0<n≦1.0であり、
Aは、下記一般式(II)、又は(III)で表される構造であり、
Bは、下記一般式(VII)で表される構造であり、
各構造単位は、ランダム共重合しており、
且つ、式(I)中の少なくとも一つのベンゼン環が少なくとも一つのスルホ基を有する。)
(上記一般式(II)または(III)において、R1~R4は、それぞれ独立に、水素及び炭素数1~3のアルキル基から選択されるか、R1とR2が一緒になって芳香環もしくは縮合芳香環を形成しかつR3とR4が一緒になって芳香環もしくは縮合芳香環を形成しているか、又はR1、R3、R4が水素でありかつR2は単結合であってcの炭素と結合しており、
Xは、単結合、又は下記式(IV)、下記式(V)若しくは下記式(VI)で表される構造であり、
Xが単結合であるとき、結合aは、Xに結合している炭素に対して、ともにオルト位置に結合しているか、又はともにメタ位置に結合しており、Xが、下記式(IV)で表される構造であるとき、結合aは、Xに結合している炭素に対してともにパラ位置に結合しており、下記式(V)で表される構造であるとき、結合aは、Xに結合している炭素に対して、ともにパラ位置に結合しているか、又はともにメタ位置に結合しており、
Xが下記式(VI)で表される構造であるとき、上記一般式(II)または(III)における結合aは一方のみであり、Aは、一方の結合aと結合bとによって、他の構造又は構造単位と結合している。)
- 燃料電池用である請求項1又は2に記載の化合物。
- 燃料電池のアノード触媒層及び/又はカソード触媒層の電解質として用いられる請求項3に記載の化合物。
- 請求項1~4のいずれか一項に記載の化合物を含む燃料電池の触媒層。
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| US16/958,509 US11312818B2 (en) | 2017-12-28 | 2018-12-27 | Polyphenylene compound |
| JP2019562196A JP7173046B2 (ja) | 2017-12-28 | 2018-12-27 | ポリフェニレン化合物 |
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| KR20240171932A (ko) * | 2023-05-30 | 2024-12-09 | 아이노머 이노베이션스, 인코포레이티드 | 이오노머 공중합체, 이의 방법, 및 용도 |
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| JP2010070750A (ja) * | 2008-08-21 | 2010-04-02 | Sumitomo Chemical Co Ltd | ポリマー、高分子電解質及びその用途 |
| WO2018187864A1 (en) * | 2017-04-10 | 2018-10-18 | Simon Fraser University | Polyphenylenes, methods, and uses thereof |
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2018
- 2018-12-27 EP EP18895067.9A patent/EP3733732B1/en active Active
- 2018-12-27 US US16/958,509 patent/US11312818B2/en active Active
- 2018-12-27 KR KR1020207021822A patent/KR102629949B1/ko active Active
- 2018-12-27 JP JP2019562196A patent/JP7173046B2/ja active Active
- 2018-12-27 WO PCT/JP2018/048300 patent/WO2019131932A1/ja not_active Ceased
- 2018-12-27 CN CN201880083994.4A patent/CN111527124B/zh active Active
- 2018-12-28 TW TW107147768A patent/TWI785177B/zh active
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| US7816482B1 (en) * | 2009-03-26 | 2010-10-19 | Sandia Corporation | Epoxy-crosslinked sulfonated poly (phenylene) copolymer proton exchange membranes |
| US8110636B1 (en) * | 2009-04-17 | 2012-02-07 | Sandia Corporation | Multi-block sulfonated poly(phenylene) copolymer proton exchange membranes |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPWO2022210641A1 (ja) * | 2021-03-31 | 2022-10-06 | ||
| WO2022210641A1 (ja) * | 2021-03-31 | 2022-10-06 | 日産化学株式会社 | スルホン酸基を有するフッ素含有化合物及び固体高分子形燃料電池 |
| EP4317242A4 (en) * | 2021-03-31 | 2024-11-20 | Nissan Chemical Corporation | FLUORINE-CONTAINING COMPOUND HAVING SULFONIC ACID GROUP AND POLYMER ELECTROLYTE FUEL CELL |
| JP7845353B2 (ja) | 2021-03-31 | 2026-04-14 | 日産化学株式会社 | スルホン酸基を有するフッ素含有化合物及び固体高分子形燃料電池 |
Also Published As
| Publication number | Publication date |
|---|---|
| TW201936694A (zh) | 2019-09-16 |
| CN111527124A (zh) | 2020-08-11 |
| KR20200103784A (ko) | 2020-09-02 |
| JP7173046B2 (ja) | 2022-11-16 |
| JPWO2019131932A1 (ja) | 2021-01-07 |
| EP3733732B1 (en) | 2025-03-26 |
| TWI785177B (zh) | 2022-12-01 |
| KR102629949B1 (ko) | 2024-01-29 |
| US11312818B2 (en) | 2022-04-26 |
| EP3733732A4 (en) | 2021-02-24 |
| CN111527124B (zh) | 2023-03-10 |
| US20210054138A1 (en) | 2021-02-25 |
| EP3733732A1 (en) | 2020-11-04 |
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