JP5614210B2 - Polymer electrolyte membrane, membrane / electrode assembly and fuel cell using the same - Google Patents

Description

The present invention relates to a polymer electrolyte membrane excellent in durability and proton conductivity, a membrane / electrode assembly using the polymer electrolyte membrane, and a fuel cell.

  In recent years, new power generation technologies with excellent energy efficiency and environmental friendliness have attracted attention. Above all, polymer electrolyte fuel cells using polymer electrolyte membranes have high energy density, and because they have features such as being easy to start and stop because of lower operating temperatures than other types of fuel cells. Developments as power supply devices for electric vehicles and distributed power generation are advancing.

  As the polymer solid electrolyte membrane, a proton conductive polymer electrolyte membrane is usually used. In addition to proton conductivity, the polymer solid electrolyte membrane must have characteristics such as fuel permeation deterrence and mechanical strength that prevent permeation of hydrogen and the like of the fuel. As such a polymer solid electrolyte membrane, for example, a membrane containing a perfluorocarbon sulfonic acid polymer into which a sulfonic acid group is introduced as represented by Nafion (registered trademark) manufactured by DuPont, USA is known.

  Perfluorocarbon sulfonic acid polymer electrolyte membranes exhibit well-balanced characteristics as electrolyte membranes for fuel cells, but more excellent membranes are required in terms of cost and performance. Fluorine polymer electrolyte membranes such as perfluorocarbon sulfonic acid polymer electrolyte membranes, when used in fuel cells, may contain harmful hydrofluoric acid in the exhaust gas depending on operating conditions, It also has problems such as giving a large load. For this reason, development of hydrocarbon-based polymer electrolyte membranes is being actively conducted.

On the other hand, in a fuel cell using hydrogen as a fuel, radicals are generated by side reactions, causing decomposition of the polymer electrolyte membrane. Hydrocarbon polymer electrolyte membranes have a problem that radical resistance is inferior to perfluorocarbon sulfonic acid polymer electrolyte membranes. The reason why the oxidation resistance is low is considered that hydrocarbon compounds generally have low durability against radicals, and electrolytes having a hydrocarbon skeleton are liable to cause deterioration reactions due to radicals (oxidation reactions due to peroxide radicals).

Therefore, various methods have been proposed for the purpose of providing a highly durable solid polymer electrolyte that has oxidation resistance equivalent to or higher than that of a fluorine-based electrolyte and that can be produced at low cost. Yes. Among these, the method of improving durability by adding an additive to the polymer electrolyte is an effective method as a simple method that can be applied to existing polymer electrolytes. A high-durability solid polymer electrolyte comprising a polymer compound having a hydrocarbon part and introduced with a functional group containing phosphorus (Patent Documents 1 and 2 below), a polymer compound having an electrolyte group and a hydrocarbon part, A highly durable solid polymer electrolyte composition obtained by mixing a phosphorus-containing polymer compound (Patent Documents 3 and 4 below) has been proposed.

  However, the method of introducing a functional group containing phosphorus has disadvantages that the polymerization of the electrolyte polymer is complicated and the structure of the electrolyte polymer that can be applied is limited. Further, in the method of mixing the polymer compound having an electrolyte group and a hydrocarbon part and the phosphorus-containing polymer compound, the phosphorus-containing polymer compound may be eluted under the operating conditions of the fuel cell.

  As a method for suppressing elution of the phosphorus-containing polymer compound, a method using a water-insoluble compound is considered. As the water-insoluble phosphorus-containing polymer compound, an aromatic polymer compound into which a functional group containing phosphorus is introduced ( The following patent documents 5 and 6) have been proposed. However, in these cases, the density of phosphorus in the polymer compound containing phosphorus is low, and in order to obtain sufficient oxidation resistance, it is necessary to add a large amount of phosphorus-containing polymer compound. There is a concern that costs will rise.

  On the other hand, it is known that phosphoric acid forms an insoluble or hardly soluble salt with many metals. As a solid polymer electrolyte composition excellent in oxidation resistance, a composite of a hydrocarbon-based solid polymer electrolyte and a zirconium phosphonate compound having a chelating functional group (Patent Document 7 below) has been filed. Although the solubility of the chelating functional group having a phosphonic acid group in water is decreased by complexing with Zr, the decrease in the solubility is not sufficient.

  From the above, it is summarized that the present applicant contains 90 to 99.95 parts by mass of an aromatic hydrocarbon polymer electrolyte, 0.05 to 10 parts by mass of a phosphorus-containing polymer compound, and 10 to 5000 ppm of a metal element. A polymer electrolyte composition (Patent Document 8 below) has been proposed. This polymer electrolyte composition has high oxidation resistance and is effective in that the phosphorus-containing polymer compound is less eluted into high-temperature water and the oxidation resistance lasts for a long time. However, the proton conductivity is equivalent or slightly lower than that of the aromatic hydrocarbon polymer electrolyte alone, which is insufficient in terms of obtaining a higher performance polymer electrolyte membrane.

JP 2000-11755 A JP 2004-79252 A JP 2000-11756 A JP 2004-134269 A JP 2003-238678 A JP 2004-175997 A JP 2002-343132 A Japanese Patent Application No. 2009-149664

  The present invention was made in the background of the problems of the prior art, and an excellent polymer electrolyte membrane capable of improving oxidation resistance and proton conductivity without causing elution of additive components, and the polymer electrolyte An object of the present invention is to provide a membrane / electrode assembly using a membrane and a fuel cell.

As a result of intensive studies, the present inventors have found that the above problems can be solved by the following means, and have reached the present invention.
That is, this invention consists of the following structures.
(1) A polymer electrolyte comprising a solid polymer electrolyte composition containing 90 to 99.95 parts by mass of an aromatic hydrocarbon polymer electrolyte, 0.05 to 10 parts by mass of a phosphorus-containing polymer compound, and 10 to 5000 ppm of a metal element. A polymer electrolyte membrane in which a composition containing a phosphorus element and a metal element existing in the polymer electrolyte membrane is uniformly dispersed with a size of 0.5 μm or less.
(2) The polymer according to (1), wherein the amount of the metal element on the surface of the polymer electrolyte membrane of the polymer electrolyte membrane is 10% or less with respect to the total addition amount and the film thickness is 5 to 30 μm. Electrolyte membrane.
(3) A film is formed from an aprotic polar solvent that dissolves a polymer electrolyte and a metal alkoxide or metal chelate compound and the polymer electrolyte, or a solution containing a mixed solvent of an aprotic polar solvent and water or alcohol (1) Or the polymer electrolyte membrane in any one of (2).
(4) manufactured from a solution containing an aprotic polar solvent that dissolves the polymer electrolyte and metal alkoxide or metal chelate compound, phosphorus-containing polymer compound and polymer electrolyte, or a mixed solvent of aprotic polar solvent and water or alcohol. The polymer electrolyte membrane according to any one of (1) and (2).
(5) The polymer electrolyte membrane according to any one of (1) to (4), wherein the phosphorus-containing polymer compound is polyvinylphosphonic acid.
(6) The metal element is one or more metal elements selected from the group consisting of Mg, Ca, Co, Ni, Zn, Sr, Zr, Ba, and Ce (1) to (5) The polymer electrolyte membrane according to any one of the above.
(7) A membrane / electrode assembly using the polymer electrolyte membrane according to any one of (1) to (6).
(8) A fuel cell using the membrane / electrode assembly according to (7).

In the present invention, the aromatic hydrocarbon polymer electrolyte is mainly composed of an aromatic hydrocarbon polymer whose main structure may contain a hetero atom such as an oxygen atom, a sulfur atom or a nitrogen atom. And having an acidic ionic group such as a sulfonic acid group, a phosphonic acid group, a sulfonimide group, a phosphoric acid group, or a carboxyl group. Further, it is preferable that the aromatic hydrocarbon polymer electrolyte is a block copolymer having a hydrophilic segment and a hydrophobic segment, because even if the ion exchange capacity is high, the swelling property against hot water is small and the durability is high.

The phosphorus-containing polymer compound includes various compounds containing a functional group containing trivalent phosphorus and / or a functional group containing pentavalent phosphorus. Moreover, as a phosphorus-containing high molecular compound, the compound which has a phosphonic acid group is preferable, and an alkylphosphonic acid type compound is especially preferable among these. In particular, polyvinyl phosphonic acid is preferably exemplified.

As the metal element, it is desirable to make the phosphorus-containing polymer compound water-insoluble or hardly soluble by interacting with the P—OH structure or the P—OH structure and the S—OH structure, and an alkaline earth metal, transition metal, And rare earth elements. In particular, Mg, Ca, Co, Ni, Zn, Sr, Zr, Ba, and Ce are preferable.

In the present invention, since the functional group containing phosphorus is introduced into the aromatic hydrocarbon polymer electrolyte, the oxidative degradation reaction of the polymer electrolyte is suppressed by the functional group containing phosphorus. Furthermore, the elution of the phosphorus-containing polymer compound can be suppressed by adding a metal element. As a result, a polymer electrolyte membrane having practically sufficient oxidation resistance can be obtained.

Furthermore, proton conductivity can be improved by uniformly dispersing the phosphorus-containing polymer compound and the metal element in the film.

The polymer electrolyte membrane according to the present invention contains an aromatic hydrocarbon-based polymer electrolyte, a phosphorus-containing polymer compound, and a metal element, so that elution of the phosphorus-containing polymer compound is suppressed and oxidation resistance is maintained for a long time. There is an effect of doing. Further, the proton conductivity is improved by uniformly dispersing the phosphorus-containing polymer compound and the metal element in the film.

FIG. 1 is a TEM photograph of the films of Example 1 and Comparative Example 4.

Hereinafter, embodiments of the present invention will be described in detail. The polymer electrolyte membrane excellent in durability and proton conductivity according to the present invention is obtained by mixing an aromatic hydrocarbon-based polymer electrolyte, a phosphorus-containing polymer compound, and a metal element.

  The aromatic hydrocarbon polymer electrolyte in the present invention needs to have an ion exchange capacity of 0.5 to 3.0 meq / g, and has an ion exchange capacity of 1.0 to 2.5 meq / g. Is preferred.

The aromatic hydrocarbon polymer electrolyte is mainly composed of an aromatic hydrocarbon polymer that may contain a hetero atom such as an oxygen atom, a sulfur atom, or a nitrogen atom. And having an acidic ionic group such as a phosphonic acid group, a sulfonimide group, a phosphoric acid group, or a carboxyl group. As the ionic group, a strong acid group such as a sulfonic acid group or a sulfonimide group is preferable because proton conductivity increases, and a phosphonic acid group or a phosphoric acid group exhibits proton conductivity even under high temperature and low humidity conditions. preferable.

The structure of the aromatic hydrocarbon polymer electrolyte in the present invention is not particularly limited, but one or more structures selected from the structure represented by the following chemical formula 1 and one structure selected from the structure represented by the following chemical formula 2 Examples of the polymer electrolyte include one or more polymers having the above structure. In Chemical Formulas 1 and 2, X is a —S (═O) ₂ — group or —C (═O) — group, Y is H or a monovalent cation, and Ar ¹ is an electron-withdrawing group. Z ¹ represents either an oxygen atom or a sulfur atom, and Ar represents one or more groups selected from the group consisting of a divalent aromatic group or a divalent aliphatic group. .

  The aromatic hydrocarbon-based polymer electrolyte in the present invention may contain a plurality of structures within the range of the structure represented by Chemical Formula 1 or 2. Moreover, the coupling | bonding mode of the structure represented by Chemical formula 1 and the structure represented by Chemical formula 2 is not specifically limited, You may couple | bond together at random, It represents with Chemical formula 1 and Chemical formula 2. A block structure in which any one of the structures is continuous, a block in which the structure represented by Chemical Formula 1 is continuous, and a block structure in which the structure represented by Chemical Formula 2 is continuous may be combined. The structure represented and the structure represented by Chemical Formula 2 may be bonded alternately. When the aromatic hydrocarbon polymer electrolyte has a block structure, even if the ion exchange capacity is increased in order to obtain high proton conductivity, the swelling property against hot water is suppressed and the durability is excellent, which is preferable.

Although the molecular weight when Chemical Formula 1 and Chemical Formula 2 have a block structure is not particularly limited, the number average molecular weight is preferably 1000 or more and 50000 or less, more preferably 2000 or more and 20000 or less, respectively.

X in Chemical Formula 1 is preferably an —S (═O) ₂ — group because solubility in a solvent is improved. It is preferable that X is a —C (═O) — group because the softening temperature of the polymer can be lowered to enhance the bonding property with the electrode, or the photocrosslinking property can be imparted to the electrolyte membrane. When used as a polymer electrolyte membrane, Y is preferably an H atom. However, if Y is an H atom, it is easily decomposed by heat or the like. Therefore, during processing such as manufacturing of an electrolyte membrane, Y is set as an alkali metal salt such as Na or K, and Y is converted to H atom by acid treatment after processing. A polymer electrolyte membrane can also be obtained by conversion. Z ¹ is preferably O since it has advantages such as less coloring of the polymer and easy availability of raw materials. Z ¹ is preferably S because oxidation resistance is improved.

  Ar in the chemical formulas 1 and 2 is one or more groups selected from the group consisting of a divalent divalent aromatic group or a divalent aliphatic group. Examples of Ar include aromatic rings such as benzene ring and pyridine ring, condensed polycyclic aromatic groups such as naphthalene ring and anthracene ring, and aromatic groups directly bonded, aliphatic groups, sulfone groups, ether groups, sulfides Groups, perfluoroalkyl groups, and groups connected by an aliphatic group including an aromatic group, aliphatic groups, and aliphatic groups including an aromatic group can be exemplified, but are not limited thereto. Absent. Ar in Chemical Formulas 1 and 2 may consist of a plurality of structures.

  Although the example of Ar in Chemical formula 1 and 2 is shown below, it is not limited to these.

Among the structures described as examples of Ar in Chemical Formulas 1 and 2, the structures of Chemical Formulas 3E and 3AV are preferable because they suppress swelling of the polymer electrolyte membrane. In addition, a structure such as chemical formulas 3F, 3G, 3N, 3O, 3U, 3Y is preferable because it lowers the softening temperature of the polymer electrolyte membrane and improves the bondability with the electrode catalyst layer. Structures represented by the chemical formulas 3AX and 3AY are also preferable because the softening temperature of the polymer electrolyte membrane is lowered, so that the bonding property with the electrode catalyst layer is improved. Furthermore, the structure represented by the chemical formulas 3AY to 3BN is preferable in order to improve the bondability with the electrode catalyst layer and improve durability, and the structure represented by the chemical formulas 3AO, 3AI, 3AN, 3AQ, 3X is This is preferable because methanol permeability is suppressed. In addition, the structures represented by the chemical formulas 3I, 3J, and 3K are preferable because they suppress flooding in the fuel cell. The structure represented by the chemical formula 3BO is preferable because it improves the durability of the polymer electrolyte membrane. In the case where Ar has a structure represented by the chemical formulas 3AY to 3BN, Z ¹ in the chemical formulas 1 and 2 is preferably a sulfur atom. O in the chemical formula 3N represents an integer of 2 to 10.

  Ar in the chemical formulas 1 and 2 may be composed of a plurality of groups. However, as a preferable combination, a structure represented by the chemical formula 3E and a chemical formula 3F, 3G, 3N, 3O, 3U, 3Y, 3AX to 3BN A combination with one or more structures selected from the group consisting of the structures represented, one or more structures selected from the group consisting of structures represented by the chemical formulas 3F, 3G, 3N, 3O, 3U, 3Y; A combination of one or more structures selected from the group consisting of structures represented by 3AY to 3BN, one or more structures selected from the group consisting of structures represented by the chemical formulas 3AO, 3AI, 3AN, 3AQ, 3X; And a combination with one or more structures selected from the group consisting of 3AY to 3BN. Further, the above-mentioned preferable structure and the combination of the preferable structures are combined with chemical formulas 3I, 3J, and 3K to obtain a flooding suppression effect, and the structure represented by chemical formula 3BO is further combined to obtain a durability improvement effect. be able to.

Ar ¹ in Chemical Formula 2 is preferably a divalent aromatic group having an electron-withdrawing group. Examples of the electron-withdrawing group include a sulfone group, a sulfonyl group, a sulfonic acid group, a sulfonic acid ester group, a sulfonic acid amide group, a sulfonic acid imide group, a carboxyl group, a carbonyl group, a carboxylic acid ester group, a cyano group, a halogen group, Although a trifluoromethyl group, a nitro group, etc. can be mentioned, it is not limited to these, What is necessary is just a well-known arbitrary electron withdrawing group.

Examples of the structure of Ar ¹ in Chemical Formula 2 are shown below, but are not limited thereto.

A preferable structure of Ar ¹ in Chemical Formula 2 is a structure represented by Chemical Formulas 4A to 4D, and among them, a structure represented by Chemical Formulas 4C and 4D is more preferable, and a structure represented by Chemical Formula 4D is more preferable. The structure of Chemical Formula 4A is preferable because it can increase the solubility of the polymer. The structure of the chemical formula 4B is preferable because it lowers the softening temperature of the polymer to improve the bondability with the electrode or impart photocrosslinkability. The structure of Chemical Formula 4C or 4D is preferable because the swelling of the polymer can be reduced, and the structure of Chemical Formula 4D is more preferable. Ar1 in Chemical Formula 2 may be composed of a plurality of structures, and when composed of a plurality of structures, it consists of two or more structures selected from the group consisting of Chemical Formulas 4A to 4D and Chemical Formulas 4A to 4D. A combination of at least one structure selected from the group and at least one structure selected from the group consisting of chemical formulas 4E to 4Q is preferable.

  The polymer constituting the polymer electrolyte in the present invention includes, for example, one or more compounds selected from the group consisting of aromatic dihalogen compounds and aromatic dinitro compounds activated with electron-withdrawing groups, bisphenol compounds, bisthiols. By heating one or more compounds selected from the group consisting of a phenol compound and an alkyldithiol compound in the presence of a basic compound, it can be polymerized by an aromatic nucleophilic substitution reaction.

By setting the molar ratio of the reactive halogen group or nitro group to the reactive hydroxy group or mercapto group in the monomer to an arbitrary molar ratio, the degree of polymerization of the resulting polymer can be adjusted. Is 0.8 to 1.2, more preferably 0.9 to 1.1, more preferably 0.95 to 1.05, and 1 to obtain a polymer with the highest degree of polymerization. Can do.

  Among aromatic dihalogen compounds activated with an electron-withdrawing group, those having an ionic group include 3,3′-disulfo-4,4′-dichlorodiphenylsulfone, 3,3′-disulfo-4, 4'-difluorodiphenyl sulfone, 3,3'-disulfo-4,4'-dichlorodiphenyl ketone, 3,3'-disulfo-4,4'-difluorodiphenyl sulfone, and their sulfonic acid groups are monovalent cations Examples include salts with seeds. The monovalent cation species may be sodium, potassium, other metal species, various amines, or the like, but is not limited thereto. Examples of the compound in which the sulfonic acid group is a salt include sodium 3,3′-disulfonate-4,4′-dichlorodiphenylsulfone, sodium 3,3′-disulfonate-4,4′-difluorodiphenylsulfone. 3,3′-sodium disulfonate-4,4′-dichlorodiphenyl ketone, 3,3′-sodium disulfonate-4,4′-difluorodiphenylsulfone, 3,3′-sodium disulfonate-4,4 ′ Difluorodiphenyl ketone, potassium 3,3′-disulfonate 4,4′-dichlorodiphenyl sulfone, potassium 3,3′-disulfonate 4,4′-difluorodiphenyl sulfone, potassium 3,3′-disulfonate 4,4 '-Dichlorodiphenyl ketone, potassium 3,3'-disulfonate 4,4'-difluorodi Examples include phenyl sulfone, potassium 3,3′-disulfonate 4,4′-difluorodiphenyl ketone, and sodium 3,3′-disulfonate-4,4′-dichlorodiphenyl sulfone, 3,3′-disulfone. Sodium acid-4,4′-difluorodiphenylsulfone is preferred.

  The activated aromatic dihalogen compound containing no ionic group includes 2,6-dichlorobenzonitrile, 2,4-dichlorobenzonitrile, 2,6-difluorobenzonitrile, 2,4-difluorobenzonitrile, 4, 4'-dichlorodiphenyl sulfone, 4,4'-difluorodiphenyl sulfone, 4,4'-difluorobenzophenone, 4,4'-dichlorobenzophenone, decafluorobiphenyl, 3,3'-bis (trifluoromethyl) -4, 4'-dichlorobiphenyl, 3,3'-bis (trifluoromethyl) -p-terphenyl, and the like, but not limited thereto, other aromatics active in aromatic nucleophilic substitution reaction Dihalogen compounds, aromatic dinitro compounds, aromatic dicyano compounds and the like can also be used. Among these, 2,6-dichlorobenzonitrile, 2,4-dichlorobenzonitrile, 2,6-difluorobenzonitrile, 2,4-difluorobenzonitrile, 2,6-dichlorobenzonitrile, 2,6 are preferable. -Difluorobenzonitrile is more preferred.

  Examples of the bisphenol compound or bisthiophenol compound include 9,9-bis (4-hydroxyphenyl) fluorene, 9,9-bis (3-methyl-4-hydroxyphenyl) fluorene, 4,4′-biphenol, 4 , 4'-dimercaptobiphenyl, bis (4-hydroxyphenyl) sulfone, 1,1-bis (4-hydroxyphenyl) ethane, 2,2-bis (4-hydroxyphenyl) propane, bis (4-hydroxyphenyl) Methane, 2,2-bis (4-hydroxyphenyl) butane, 3,3-bis (4-hydroxyphenyl) pentane, 2,2-bis (4-hydroxy-3,5-dimethylphenyl) propane, bis (4 -Hydroxy-3,5-dimethylphenyl) methane, bis (4-hydroxy-2,5-dimethylphenyl) Methane, bis (4-hydroxyphenyl) phenylmethane, bis (4-hydroxyphenyl) diphenylmethane, 1,1-bis (4-hydroxyphenyl) cyclohexane, 4-hexyl resorcinol, 2,2-bis (4-hydroxyphenyl) Hexafluoropropane, hydroquinone, resorcin, bis (4-hydroxyphenyl) ketone, 4,4′-thiodiphenol, 4,4′-oxydiphenol, 1,3-bis (4-hydroxyphenyl) adamantane, 2, 2-bis (4-hydroxyphenyl) adamantane, 4,4′-thiobisbenzenethiol, 1,3-benzenedithiol, 1,4-benzenedithiol, 10- (2,5-dihydroxyphenyl) -9,10- Dihydro-9-oxa-10-phosphaphenant -10-oxide, 4,4′-biphenol, 9,9-bis (4-hydroxyphenyl) fluorene, 1,3-bis (4-hydroxyphenyl) adamantane, 4,4′-thiodiphenol, 4, 4′-oxydiphenol, 4,4′-thiobisbenzenethiol, 4-ethylresorcinol, 4-hexylresorcinol, 2-hexylhydroquinone, 2-octylhydroquinone, 2-octadadecylhydroquinone, 2-tertiarybutylhydroquinone, 2,5-ditertiary butyl hydroquinone, 2,5-ditertiary amyl hydroquinone, 2,2′-dihexyl-4,4′-dihydroxybiphenyl, 1-octyl-2,6-dihydroxynaphthalene, 2-hexyl-1, 5-dihydroxynaphthalene, etc. However, the present invention is not limited thereto, and any compound that can react with the aromatic dihalogen compound or aromatic dinitro compound activated with the electron-withdrawing group can be used.

  Examples of alkyldithiol compounds include 1,2-ethanedithiol, 1,3-propanedithiol, 1,2-propanedithiol, 1,4-butanedithiol, 2,3-dihydroxy-1,4-butanedithiol, , 5-pentanedithiol, 1,6-hexanedithiol, 1,7-heptanedithiol, 1,8-octanedithiol, 1,9-nonanedithiol, 1,10-decanedithiol, 1,11-undecanedithiol, 1, 12-dodecanedithiol, 1,13-tridecanedithiol, 1,14-tetradecanedithiol, 1,15-pentadecanedithiol, 1,16-hexadecanedithiol, 1,17-heptadecanedithiol, 1,18-octadecanedithiol, 1 , 19-nonadecanedithiol, 1,20- Cosanedithiol, 3,6-dioxa-1,8-octanedithiol, 3,7-dithia-1,9-nonanedithiol, 3-thia-1,5-pentanedithiol, 2,3-dihydroxy-1,4- Examples include butanedithiol, 1,4-bis (mercaptomethyl) benzene, 1,3-bis (mercaptomethyl) benzene, 1,2-bis (mercaptomethyl) benzene, and the like. Any compound that can react with an aromatic dihalogen compound or an aromatic dinitro compound activated with an electron-withdrawing group can be used.

  The polymerization can be carried out in the temperature range of 0 to 350 ° C., but is preferably 50 to 250 ° C. When the temperature is lower than 0 ° C., the reaction does not proceed sufficiently, and when the temperature is higher than 350 ° C., the polymer tends to be decomposed. The reaction can be carried out in the absence of a solvent, but is preferably carried out in a solvent. Examples of the solvent that can be used include N-methyl-2-pyrrolidone, N, N-dimethylacetamide, N, N-dimethylformamide, dimethyl sulfoxide, diphenyl sulfone, sulfolane, and the like. And any solvent that can be used as a stable solvent in the aromatic nucleophilic substitution reaction. These organic solvents may be used alone or as a mixture of two or more.

  In the above polymerization reaction, a bisphenol compound, a bisthiophenol compound, and an alkyldithiol compound are reacted with an isocyanate compound such as phenyl isocyanate without using a basic compound, and an activated dihalogen aromatic A compound or a dinitroaromatic compound can also be directly reacted.

  Examples of basic compounds include sodium hydroxide, potassium hydroxide, sodium carbonate, potassium carbonate, sodium hydrogen carbonate, potassium hydrogen carbonate, etc., which can convert aromatic diols and aromatic dimercapto compounds into an active phenoxide structure. If it is, it can be used without being limited to these. The basic compound can be polymerized satisfactorily when used in an amount of 100 mol% or more as an alkali metal with respect to the hydroxyl group and mercapto group of the bisphenol compound, bisthiophenol compound, and alkyldithiol compound, It is the range of 105-125 mol% as an alkali metal with respect to the hydroxyl group and mercaptoto group of a bisphenol compound, a bisthiophenol compound, and an alkyldithiol compound. An excessive amount of the basic compound is not preferable because it causes side reactions such as decomposition.

  In the aromatic nucleophilic substitution reaction, water may be generated as a by-product. In this case, regardless of the polymerization solvent, water can be removed from the system as an azeotrope by coexisting toluene or the like in the reaction system. As a method for removing water out of the system, a water absorbing material such as molecular sieve can also be used. When the aromatic nucleophilic substitution reaction is carried out in a solvent, it is preferable to charge the monomer so that the resulting polymer concentration is 5 to 50% by weight. When the amount is less than 5% by weight, the degree of polymerization tends to be difficult to increase. On the other hand, when the amount is more than 50% by weight, the viscosity of the reaction system becomes too high, and the post-treatment of the reaction product tends to be difficult. After completion of the polymerization reaction, the solvent is removed from the reaction solution by evaporation, and the residue is washed as necessary to obtain the desired polymer. In addition, the polymer can be obtained by precipitating the polymer as a solid by adding the reaction solution in a solvent having low polymer solubility, and collecting the precipitate by filtration. In addition, a polymer solution can be obtained by removing by-product salts by filtration.

The solid polymer electrolyte of the present invention has a block structure in which any one of the structures represented by Chemical Formula 1 and Chemical Formula 2 is continuous, or a structure in which the structure represented by Chemical Formula 1 is continuous and a structure represented by Chemical Formula 2. Although the form which the continuous block structure couple | bonded may be sufficient, the formation method of such a block structure is not specifically limited. For example, a polymer having a segment represented by Chemical Formula 1 and having a hydroxyl group or a halogeno group at both ends or a hydroxyl group at one end of the hydroxyl group and a segment represented by Chemical Formula 2 However, it can be prepared by reacting in combination with a polymer in which both ends are hydroxy groups or halogeno groups or one end is a hydroxy group and the other is a halogeno group.

  For example, a. A method in which a polymer having hydroxy groups at both ends and a polymer having halogeno groups at both ends are condensed by an aromatic nucleophilic substitution reaction under the action of a base; b. A method in which a polymer having one hydroxy group and one halogeno group at both ends and another polymer having one hydroxy group and one halogeno group at both ends are condensed by an aromatic nucleophilic substitution reaction under the action of a base, c . A polymer having a hydroxy group at both ends and another polymer having a hydroxy group at both ends serve as a linking group such as 4,4′-difluorobenzophenone, decafluorobiphenyl, hexafluorobenzene, and 4,4′-difluorodiphenylsulfone. A method of binding using a compound, d. A polymer having a halogeno group at both ends and another polymer having a halogeno group at both ends are linked to 4, 4′-dihydroxybiphenyl, bisphenol A, 4,4′-dihydroxybenzophenone, 4,4′-dihydroxydiphenyl sulfone, etc. Examples thereof include a method of using a compound acting as a group or bonding by a dehalogen condensation reaction. Moreover, the method of carrying out the polymerization reaction of the polymer and monomer which have the reactive group which can cause the elementary reaction similar to the said reaction can also be used.

  The aromatic hydrocarbon polymer electrolyte used for the composite polymer electrolyte membrane of the present invention preferably has a logarithmic viscosity of 0.1 dL / g or more measured by a method described later. When the logarithmic viscosity is less than 0.1 dL / g, the membrane tends to become brittle when molded as a polymer electrolyte membrane. The logarithmic viscosity is more preferably 0.3 dL / g or more. On the other hand, when the logarithmic viscosity exceeds 5 dL / g, problems in processability such as difficulty in dissolving the polymer occur, which is not preferable. As a solvent for measuring the logarithmic viscosity, polar organic solvents such as N-methylpyrrolidone and N, N-dimethylacetamide can be generally used. When the solubility in these is low, concentrated sulfuric acid is used. It can also be measured.

  The composite polymer electrolyte membrane in the present invention can have any thickness, but if it is 5 μm or less, it becomes difficult to satisfy the predetermined characteristics, so it is preferably 5 μm or more, and more preferably 7 μm or more. . Moreover, since manufacture will become difficult when it becomes 100 micrometers or more, it is preferable that it is 100 micrometers or less, and it is more preferable that it is 30 micrometers or less.

  The composite polymer electrolyte membrane composition in the present invention may contain other polymers. Examples of such polymers include polyesters such as polyethylene terephthalate, polybutylene terephthalate, and polyethylene naphthalate, polyamides such as nylon 6, nylon 6,6, nylon 6,10, and nylon 12, polymethyl methacrylate, and polymethacrylic acid. Acrylate resins such as esters, polymethyl acrylate, polyacrylates, polyacrylic acid resins, polymethacrylic acid resins, polyethylene, polypropylene, various polyolefins including polystyrene and diene polymers, polyurethane resins, cellulose acetate Cellulose resins such as ethyl cellulose, polyarylate, aramid, polycarbonate, polyphenylene sulfide, polyphenylene oxide, polysulfone, polyethylene Thermal curing of aromatic polymers such as tersulfone, polyetheretherketone, polyetherimide, polyimide, polyamideimide, polybenzimidazole, polybenzoxazole, polybenzthiazole, epoxy resin, phenol resin, novolac resin, benzoxazine resin There are no particular restrictions on the conductive resin. A resin composition with a basic polymer such as polybenzimidazole or polyvinylpyridine can be said to be a preferable combination for improving the polymer dimensionality, and when a sulfonic acid group is further introduced into these basic polymers, The processability of the composition becomes more preferable. The polymer electrolyte membrane of the present invention preferably contains 50% by mass or more and less than 100% by mass of the proton conductive polymer. More preferably, it is 70 mass% or more and less than 100 mass%. If it is less than 50% by weight, the sulfonic acid group concentration of the polymer electrolyte membrane tends to be low, and good ionic conductivity tends to be not obtained, and the unit containing the sulfonic acid group becomes a discontinuous phase and conducts. Ion mobility tends to decrease. The polymer electrolyte membrane of the present invention can be used as necessary, for example, an antioxidant, a heat stabilizer, a lubricant, a tackifier, a plasticizer, a crosslinking agent, a viscosity modifier, an antistatic agent, an antibacterial agent, and an antifoaming agent. Various additives such as an agent, a dispersant, and a polymerization inhibitor may be included.

In the present invention, the phosphorus-containing polymer compound means a polymer compound containing a functional group containing phosphorus, and corresponds to a polymer compound having a functional group containing phosphorus in the main chain or side chain. The functional group containing phosphorus includes a functional group containing trivalent phosphorus and a functional group containing pentavalent phosphorus. The “functional group containing phosphorus” in the present invention includes trivalent and functional groups. Both pentavalent functional groups are included. These functional groups containing phosphorus are represented by the general formulas shown in the following chemical formula 6 (functional group containing trivalent phosphorus) and chemical formula 7 (functional group containing pentavalent phosphorus). Can do.

In the formulas 6 and 7, x, y, and z take a value of 0 or 1. In the formulas 7 and 8, R ₁ represents a linear, cyclic, or branched hydrocarbon compound represented by the general formula CmHn, or R 2 and R 3 represent fluorine, chlorine, bromine. A halogen atom or a hydrogen atom, or a monovalent organic group. Further, in the formulas 6 and 7, when y or z is 1, R ₂ or R ₃ may be a metal atom.

Specific examples of the functional group containing phosphorus include phosphonic acid groups, phosphonic acid ester groups, phosphite groups, phosphoric acid, and phosphoric acid esters. Among these, a phosphonic acid group is particularly suitable as a functional group containing phosphorus because it is inexpensive and can impart high oxidation resistance to a polymer compound having a hydrocarbon moiety.

Specific examples of the phosphorus-containing polymer compound include polyvinyl phosphonic acid, a copolymer containing polyvinyl phosphonic acid, a polyether sulfone resin into which a phosphonic acid group is introduced, a polyether ether ketone resin, a linear phenol- Formaldehyde resin, cross-linked phenol-formaldehyde resin, linear polystyrene resin, cross-linked polystyrene resin, linear poly (trifluorostyrene) resin, cross-linked (trifluorostyrene) resin, poly (2,3-diphenyl-1 , 4-phenylene oxide) resin, poly (allyl ether ketone) resin, poly (arylene ether sulfone) resin, poly (phenylquinosan phosphorus) resin, poly (benzyl silane) resin, polystyrene-graft-ethylenetetrafluoroethylene resin, Polystyrene graph - polyvinylidene fluoride resins, polystyrene - graft - tetrafluoroethylene resin and the like as an example.

The method for mixing the aromatic hydrocarbon polymer electrolyte and the phosphorus-containing polymer compound is not particularly limited, and various methods can be used. For example, a solution dope or blend may be used. Further, when both the aromatic hydrocarbon polymer electrolyte and the phosphorus-containing polymer compound are heat-melted, they may be blended by heat melting.

Alternatively, the structure may be such that the phosphorus-containing polymer compound is uniformly dispersed throughout the solid polymer electrolyte by uniformly mixing the aromatic hydrocarbon polymer electrolyte and the phosphorus-containing polymer compound. Alternatively, the main part of the solid polymer electrolyte is composed only of the aromatic hydrocarbon polymer electrolyte, and only the part requiring oxidation resistance is a mixture of the aromatic hydrocarbon polymer electrolyte and the phosphorus-containing polymer compound. You may comprise.

For example, in an environment where radicals are randomly generated in the membrane, such as when the solid polymer electrolyte membrane is heated while immersed in a peroxide solution, the aromatic hydrocarbon polymer electrolyte and the phosphorus-containing A structure in which a molecular compound is uniformly mixed and a phosphorus-containing polymer compound is uniformly dispersed in a solid polymer electrolyte membrane is effective.

On the other hand, in an environment where a peroxide is generated in the catalyst layer on the surface of the membrane, such as an electrolyte membrane for water electrolysis or fuel cell, and the generated peroxide diffuses into a peroxide radical to cause a degradation reaction. It is not necessary that the phosphorus-containing polymer compound is uniformly dispersed in the film. In this case, by doping the aromatic hydrocarbon polymer electrolyte with a phosphorus-containing polymer compound, only the surface portion of the membrane having the most oxidative degradation reaction is mixed with the aromatic hydrocarbon polymer electrolyte and the phosphorus-containing polymer electrolyte. A mixture of polymer compounds may be used.

Alternatively, a method of inserting a membrane-like molded product made of a mixture of an aromatic hydrocarbon polymer electrolyte and a phosphorus-containing polymer compound between an electrolyte consisting only of an aromatic hydrocarbon polymer electrolyte and an electrode is also available. It is considered effective for maintaining the performance of

In addition, the type and amount of the electrolyte group to be introduced into the aromatic hydrocarbon polymer electrolyte, or the mixing ratio of the phosphorus-containing polymer compound and the aromatic hydrocarbon polymer electrolyte can be determined by conductivity, oxidation resistance, etc. It may be adjusted according to the characteristics required for the solid polymer electrolyte membrane and the compatibility of the aromatic hydrocarbon polymer electrolyte and the phosphorus-containing polymer compound.

That is, as the amount of the phosphorus-containing polymer compound introduced increases, the oxidation resistance improves. However, when the amount of the phosphorus-containing polymer compound introduced is increased, the aromatic hydrocarbon polymer electrolyte and the phosphorus-containing polymer compound cannot form a uniform solution, making film formation difficult. Particles larger than 0.5 μm can be formed, and the membrane becomes fragile. In order to maintain the physical properties of the film, the phosphorus-containing polymer compound particles are more preferably 0.3 μm or less.

However, when the amount of the polymer compound containing phosphorus is less than 0.05 parts by mass of the polymer electrolyte composition, the effect of improving the oxidation resistance is not sufficient. Therefore, the amount of the polymer compound containing phosphorus needs to be 0.05 parts by mass or more of the total electrolyte group. In particular, in the case of a solid polymer electrolyte used under severe conditions such as a fuel cell, water electrolysis, and salt electrolysis, the functional group containing phosphorus is preferably 0.3 parts by mass or more. Further, when the amount of the phosphorus-containing polymer compound introduced exceeds 10 parts by mass of the polymer electrolyte composition, the physical properties of the membrane deteriorate. Accordingly, the amount of the phosphorus-containing polymer compound introduced must be less than 10 parts by mass of the total electrolyte.

In the present invention, the polymer electrolyte membrane composition is characterized by containing 10 to 5000 ppm of a metal element. Preferred metal elements include a P—OH structure or an interaction between a P—OH structure and an S—OH structure. Thus, it is desirable to make the phosphorus-containing polymer compound water-insoluble or sparingly soluble, and examples thereof include alkaline earth metals, transition metals, and rare earth elements. In particular, Mg, Ca, Co, Ni, Zn, Sr, Zr, Ba, and Ce are preferable.

The composite polymer electrolyte membrane composition in the present invention may contain only one of the above-described metal elements, or may contain two or more metal elements.

If the amount of the metal element is not 10 ppm or more based on the electrolyte composition, the elution suppressing effect of the phosphorus-containing polymer compound is not sufficient, and if it exceeds 5000 ppm, the proton conductivity decreases, and the characteristics of the fuel cell membrane as an electrolyte Is unfavorable because of lowering. A preferable content is 50 ppm or more and 5000 ppm or less.

Even if the amount of the metal element added is 5000 ppm or less, it is not preferable that the metal element is biased on the surface of the film because proton conduction is inhibited. When the content of the metal element is 10 to 5000 ppm, in the composition analysis of the film surface by X-ray photoelectron analysis (XPS), the atom% of the metal element is preferably 0.5 or less, and is 0.2 or less. Is more preferable.

As mentioned above, the effect of adding the metal element is to suppress the elution of the phosphorus-containing polymer compound into the water. Elution of the molecular compound into water is 10% by mass or less even when immersed for 48 hours at 80 ° C.

Moreover, the effect of improving proton conductivity can be obtained by uniformly dispersing the phosphorus-containing polymer compound and the metal element in the film. The reason why the proton conductivity is improved is not clear, but it is considered that the density of acid groups increases due to proton conduction by metal phosphate and phosphonic acid groups. Here, uniform distribution refers to the result of determination by the method described in the examples described later.

Various methods can be used for mixing the metal elements. In order to uniformly disperse the metal elements throughout the film, the metal elements are included in the solution containing the aromatic hydrocarbon polymer electrolyte before film formation. A method of adding a compound is desirable. For example, a method in which a compound containing a metal element or a solution thereof is added to and mixed with a solution in which an aromatic hydrocarbon polymer electrolyte is dissolved in a suitable solvent, and then a phosphorus-containing polymer compound or a solution thereof is added. . Alternatively, a method of adding a phosphorus-containing polymer compound or a solution thereof to a solution in which an aromatic hydrocarbon-based polymer electrolyte is dissolved in an appropriate solvent and mixing the mixture, and then adding the compound containing the metal element or the solution thereof. . Alternatively, a phosphorus-containing polymer compound or a solution thereof and a compound containing a metal element or a solution thereof may be mixed to prepare a phosphorus-containing compound and metal composite, and then mixed with an aromatic hydrocarbon polymer electrolyte. . Also, an electrolyte of a mixture of a hydrocarbon polymer electrolyte and a metal element prepared by adding a compound containing a metal element or a solution thereof to a solution in which an aromatic hydrocarbon polymer electrolyte is dissolved in a suitable solvent. Membrane or precursor thereof, catalyst layer or diffusion layer, or electrolyte membrane of aromatic hydrocarbon polymer electrolyte and metal element mixture having catalyst layer formed on its surface or precursor thereof, diffusion layer or polyethylene A method of bringing a substrate such as terephthalate into contact with a solution containing a phosphorus-containing polymer compound may also be used. When mixing metal elements by these methods, cooling or overheating may be performed as necessary.

Phosphorus-containing polymer compound or metal element may be doped and mixed with the sulfonic acid group of the polymer electrolyte membrane forming a salt with the cationic species, and converted to free sulfonic acid group by acid treatment In this state, a phosphorus-containing polymer compound or a metal element may be doped and mixed.

  The compound containing a metal element is not particularly limited as long as it is uniformly mixed with an aromatic hydrocarbon electrolyte solution and does not cause precipitation. Metal alkoxide or metal chelate compound is preferable.

  The metal alkoxide is not particularly limited, but metal alkoxides of Mg, Ca, Co, Ni, Zn, Sr, Zr, Ba, and Ce are preferable, and Zr is particularly preferable. As an alkoxyl group, Preferably it is a C1-C10 alkoxyl group, More preferably, a C2-C4 alkoxyl group is mentioned. Specifically, methoxy group, ethoxy group, n-propyloxy group, isopropyloxy group, n-butyloxy group, sec-butyloxy group, tert-butyloxy group, isobutyloxy group, n-pentyloxy group Examples include a 2,2-dimethylpropyloxy group, a cyclopentyloxy group, an n-hexyloxy group, a cyclohexyloxy group, a 2-methylpentyloxy group, or a 2-ethylhexyloxy group.

  The alkoxyl group may have a substituent, and examples of the substituent include a halogen atom, an alkoxyl group, an alkylthio group, an ester group, and an acyl group.

  The metal chelate compound is not particularly limited, but metal alkoxides of Mg, Ca, Co, Ni, Zn, Sr, Zr, Ba, and Ce are preferable, and Zr is particularly preferable. Examples of chelating groups include acetoacetic esters (such as ethyl acetoacetate), 1,3-diketones (such as acetylacetone), acetoacetamides (such as N, N′-dimethylaminoacetoacetamide), and the like. preferable.

  Solvents used for dissolving a compound containing a metal element include N, N-dimethylformamide, N, N-dimethylacetamide, N, N-diethylacetamide, N-methyl-2-pyrrolidone, dimethyl sulfoxide, hexamethylphosphonamide , Polar solvents such as aprotic organic polar solvents such as N-morpholine oxide, alcohol solvents such as methanol and ethanol, ketone solvents such as acetone, ether solvents such as diethyl ether, and these organic solvents A mixture as well as a mixture with water can be mentioned, but not limited thereto.

When a metal alkoxide is used, a chemical modifier that can be chelated to a metal atom may be used for the purpose of controlling the reactivity to the phosphorus-containing polymer compound or the aromatic hydrocarbon electrolyte. Examples of the chemical modifier include acetoacetic esters (such as ethyl acetoacetate), 1,3-diketones (such as acetylacetone), and acetoacetamides (such as N, N′-dimethylaminoacetoacetamide). . When these chemical modifiers are used, 0. 1-3.5 equivalent is preferable, More preferably, it is 0.5-3 equivalent.

Furthermore, an acid or an alkali may be used as a catalyst for controlling the reaction with the phosphorus-containing polymer compound or the aromatic hydrocarbon electrolyte. As the alkali, alkali metal hydroxide such as sodium hydroxide, ammonia and the like are generally used. An inorganic or organic proton acid can be used as the acid catalyst. Examples of the inorganic protonic acid include hydrochloric acid, sulfuric acid, boric acid, nitric acid, perchloric acid, tetrafluoroboric acid, hexafluoroarsenic acid, hydrobromic acid and the like.
Examples of the organic protonic acid include acetic acid, oxalic acid, methanesulfonic acid and the like. Since the solubility of the metal compound in the solvent varies depending on the amount of the acid, it must be adjusted so that the metal compound has a soluble solubility. 0 0 0 1 to 1 equivalent is preferred.

  In addition, after doping and mixing the phosphorus-containing polymer compound or metal element, in order to remove the excess phosphorus-containing polymer compound or metal element, washing with ion-exchanged water may be performed at any stage. At this time, heat may be applied as necessary.

  In any of the methods, when there is no problem with the remaining, elution, etc. of the excessive phosphorus-containing polymer compound or metal element, washing with ion-exchanged water may be omitted.

  Examples of the solvent that can be used in the solution composition for producing the polymer electrolyte membrane of the present invention include N, N-dimethylformamide, N, N-dimethylacetamide, N, N-diethylacetamide, and N-methyl-2. -Aprotic organic polar solvents such as pyrrolidone, dimethyl sulfoxide, hexamethylphosphonamide, N-morpholine oxide, alcohol solvents such as methanol and ethanol, ketone solvents such as acetone, ether solvents such as diethyl ether, etc. Examples include, but are not limited to, polar solvents, mixtures of these organic solvents, and mixtures with water.

  The concentration of the polymer electrolyte in the solution composition is preferably in the range of 0.1 to 50% by weight, more preferably in the range of 3 to 50% by weight, and still more preferably in the range of 5 to 30% by weight.

  The most preferable method for forming the polymer electrolyte membrane of the present invention is casting from a solution composition, and the polymer electrolyte membrane can be obtained by removing the solvent from the cast solution composition as described above. . The removal of the solvent is preferably by drying in view of the uniformity of the polymer electrolyte membrane. Moreover, in order to avoid decomposition | disassembly and alteration of a compound or a solvent, it can also dry at the lowest temperature possible under reduced pressure. Moreover, when the viscosity of a solution composition is high, when a board | substrate and a solution are heated and cast at high temperature, the viscosity of a solution composition will fall and it can cast easily. The thickness of the solution composition at the time of casting is not particularly limited, but is preferably 10 to 2000 μm. More preferably, it is 50-1500 micrometers. When the thickness of the solution composition is less than 10 μm, the form as a polymer electrolyte membrane tends not to be maintained, and when it is more than 2000 μm, a non-uniform film tends to be easily formed. A known method can be used as a method for controlling the cast thickness of the solution composition. For example, the thickness can be controlled by the amount and concentration of the solution by making the thickness constant using an applicator, a doctor blade or the like, or making the cast area constant using a glass petri dish or the like. The cast solution composition can obtain a more uniform film by adjusting the solvent removal rate. For example, in the case of heating, the evaporation rate can be reduced by lowering the temperature in the first stage. In addition, when immersed in a non-solvent such as water, the coagulation rate of the compound can be adjusted by leaving the solution composition in air or an inert gas for an appropriate time. When processing is accompanied by heating, it is preferable that the sulfonic acid group in the proton conductive polymer forms a salt with a cation because stability is improved. However, for use as a polymer electrolyte membrane, it can be converted to free sulfonic acid by an appropriate acid treatment. In this case, it is effective to immerse the membrane in an aqueous solution of sulfuric acid, hydrochloric acid, etc. with or without heating.

The membrane / electrode assembly of the present invention can be obtained by bonding the composite polymer electrolyte membrane of the present invention to an electrode catalyst layer.
An electrode consists of an electrode material and a layer (electrode catalyst layer) containing a catalyst formed on the surface thereof, and a known material can be used as the electrode material. For example, a conductive porous material such as carbon paper or carbon cloth can be used, but is not limited thereto. As the conductive porous material such as carbon paper or carbon cloth, a material subjected to surface treatment such as water repellent treatment or hydrophilic treatment can be used. A known material can be used for the catalyst. For example, platinum, an alloy of platinum and ruthenium, and the like can be given, but the invention is not limited to them.
The catalyst can be used in any known form, and for example, carbon particles carrying catalyst fine particles can be used, but are not limited thereto.
An adhesive can be used for the catalyst and the electrode catalyst layer including the particles carrying the catalyst, and as the adhesive, a resin having proton conductivity can be used.

  As a method for producing this joined body, a conventionally known method can be used. For example, a method of applying an adhesive to the electrode surface and bonding the composite polymer electrolyte membrane and the electrode, a composite polymer electrolyte membrane And a method of heating and pressurizing the electrode catalyst layer prepared by applying a paste containing a catalyst to the electrode in advance, attaching the electrode after transferring the catalyst layer prepared on another sheet to the composite polymer electrolyte membrane Examples of the method include, but are not limited to, a method in which a dispersion containing a catalyst and conductive particles is coated on the surface of the composite polymer electrolyte membrane by spraying, printing, or the like, and then joining the electrodes. As the adhesive, a known material such as a Nafion (trade name) solution may be used, or an adhesive mainly composed of the same polymer composition as that of the polymer constituting the polymer electrolyte in the present invention may be used. Those having other hydrocarbon proton conductive polymers as a main component may also be used. The catalyst such as platinum and platinum-ruthenium alloy necessary for the electrode reaction can be obtained by dispersing the catalyst supported on conductive particles such as carbon in the adhesive. .

  The fuel cell of the present invention can be produced using the composite polymer electrolyte membrane or the membrane / electrode assembly of the present invention. The fuel cell of the present invention includes, for example, an oxygen electrode, a fuel electrode, a polymer electrolyte membrane sandwiched between the electrodes, an oxidant flow path provided on the oxygen electrode side, and a fuel electrode side. The fuel flow path is provided. A fuel cell stack can be obtained by connecting such unit cells with a conductive separator.

  The composite polymer electrolyte membrane of the present invention is suitable for a polymer electrolyte fuel cell. The solid polymer electrolyte membrane of the present invention is excellent in oxidation resistance and proton conductivity due to the phosphorus-containing polymer compound, and excellent in long-term durability by suppressing elution of the phosphorus-containing polymer compound. The composite polymer electrolyte membrane of the present invention can be used for a fuel cell that uses a liquid such as methanol, dimethyl ether, or formic acid as a fuel, but can be particularly suitably used for a fuel cell that uses a gas such as hydrogen. Further, it can be used for any known application as a polymer electrolyte membrane such as an electrolytic membrane and a separation membrane.

  EXAMPLES Hereinafter, although this invention is demonstrated concretely using an Example, this invention is not limited to these Examples. Various measurements were performed as follows.

<Solution viscosity>
The polymer powder was dissolved in N-methyl-2-pyrrolidone (abbreviation: NMP) at a concentration of 0.5 g / dL, and the viscosity was measured using a Ubbelohde viscometer in a constant temperature bath at 30 ° C. [Ta / tb]) / c (ta represents the sample solution dropping time, tb represents the solvent dropping time, and c represents the polymer concentration).

<Proton conductivity>
A platinum wire (diameter: 0.2 mm) was pressed against the surface of the strip-shaped membrane sample on a self-made measuring probe (manufactured by Teflon (registered trademark)), and a constant temperature / humidity oven at 80 ° C. and 95% RH (Nagano Science Co., Ltd. The sample was held in Machine Works, LH-20-01), and the impedance between the platinum wires was measured by SOLARTRON 1250 FREQUENCY RESPONSE ANALYSER. The measurement was performed while changing the distance between the electrodes, and the conductivity obtained by canceling the contact resistance between the film and the platinum wire was calculated from the gradient obtained by plotting the distance measured between the electrodes and the resistance measurement value estimated from the CC plot.
Conductivity [S / cm] = 1 / film width [cm] × film thickness [cm] × resistance interelectrode gradient [Ω / cm]

<Evaluation of power generation>
It becomes uniform after adding commercially available 40% Pt catalyst-supporting carbon (Tanaka Kikinzoku Kogyo Co., Ltd. Fuel Cell Catalyst TEC10V40E), a small amount of ultrapure water and isopropanol to a DuPont 20% Nafion (trade name) solution. To prepare a catalyst paste. This catalyst paste was uniformly applied to Toray carbon paper TGPH-060 so that the amount of platinum deposited was 0.5 mg / cm ² and dried to prepare a gas diffusion layer with an electrode catalyst layer. By sandwiching the polymer electrolyte membrane between the gas diffusion layers with the electrode catalyst layer so that the electrode catalyst layer is in contact with the membrane, and pressurizing and heating at 160 ° C. and 10 MPa for 3 minutes by a hot press method, A membrane-electrode assembly was obtained. The joined body was assembled in an evaluation fuel cell FC25-02SP manufactured by Electrochem, and hydrogen and air humidified at 75 ° C. were supplied to the anode and the cathode at a cell temperature of 80 ° C., and the power generation characteristics were evaluated. The output voltage at a current density of 0.5 A / cm ² was defined as electric power (V).

<NMR measurement>
The polymer (the sulfonic acid group is Na or K salt) was dissolved in a solvent, and ¹ H-NMR measurement was performed at room temperature using a VARIAN UNITY-500. As the solvent, a mixed solvent of NMP and deuterated dimethyl sulfoxide (85/15 vol./vol.) Was used. The hydrophilic oligomer and the hydrophobic oligomer constituting the hydrophilic segment and the hydrophobic segment of the block polymer are measured by measuring the ¹ H-NMR spectrum, and from the integration ratio of the peak derived from the end group and the peak of the skeleton part, The average molecular weight was determined. Also, the block polymer was analyzed and the composition ratio of the hydrophilic segment and hydrophobic segment in ^{1 H-NMR.}

<Swellability evaluation>
A polymer electrolyte membrane that had been left in a room at 23 ° C. and 50% RH for one day was cut into a 50 mm square and immersed in hot water at 80 ° C. for 24 hours. After soaking, the dimensions and weight of the membrane were quickly measured. The membrane was dried at 120 ° C. for 3 hours, and the dry weight was measured. The water absorption rate and area swelling rate were calculated according to the following formula. The size of the film was measured by measuring the length of two orthogonal sides connected to a specific vertex.
Water absorption (%) = {weight after immersion (g) −dry weight (g)} ÷ dry weight (g) × 100
Area swelling ratio (%) = {side length A (mm) after immersion × side length B (mm) after immersion} ÷ {50 × 50} × 100-100

<Quantitative analysis of phosphorus>
The polymer electrolyte membrane was dried in a vacuum dryer (110 ° C.) for 8 hours, and then allowed to cool to room temperature in a desiccator. Part of the sample was weighed into a 50 ml Erlenmeyer flask, sulfuric acid (97%, for precision analysis) 3 ml, nitric acid (60%, for precision analysis) 3.5 ml, perchloric acid (60%, for precision analysis) 0.5 ml Then, the temperature was gradually raised on a hot plate to cause acid decomposition. Finally, heating was continued until white sulfuric acid smoke was confirmed, and nitric acid and perchloric acid were removed. Neutralization treatment was performed using ammonia water, and the molybdic acid and phosphoric acid in the decomposition solution were reacted to form phosphomolybdic acid, which was reduced by hydrazine sulfate, and the absorbance at 830 nm of heteropolyblue produced was quantified. . The quantification was performed separately using a calibration curve obtained using a phosphorus standard solution.

<Quantitative analysis of zirconium>
The polymer electrolyte membrane was dried in a vacuum dryer (110 ° C.) for 8 hours, and then allowed to cool to room temperature in a desiccator. A part of the sample was weighed into a platinum crucible, heated and carbonized on a hot plate, and after carbonization, heated in an electric furnace (550 ° C.) overnight to incinerate. To the incineration residue, 5 ml of hydrochloric acid (6M) and several drops of hydrofluoric acid (50%) were added, and heat treatment (100 ° C.) was performed on a hot plate. After the acid volatilized, 20 ml of hydrochloric acid (1.2 M) was added and allowed to stand overnight to completely dissolve the inorganic matter. The amount of zirconium in the solution was determined by a calibration curve method using an ICP emission spectrometer.

<Quantitative analysis of cerium>
The sample was dried in a vacuum dryer (110 ° C.) for 8 hours, and then allowed to cool to room temperature in a desiccator. A part of the sample was weighed in a Teflon (registered trademark) container for closed-system acid decomposition, 4 ml of nitric acid (60%, for precision analysis) was added, and heat acid decomposition was performed in a microwave decomposition apparatus. After confirming the complete decomposition, the solution was diluted to a constant volume of 30 ml using purified water. About the amount of cerium in a measuring liquid, it calculated | required with the analytical curve method using the ICP emission spectrometer.

<Dissolution test of phosphorus-containing compounds>
The polymer electrolyte membrane was immersed in an excess amount of water 500 times or more by weight, and heated in an oven at 80 ° C. for 48 hours. A sample was taken out and air-dried, followed by quantitative analysis of phosphorus. The elution amount of the phosphorus-containing compound was determined from the following formula.
Dissolution amount (%) = (Amount of phosphorus before dissolution test−Amount of phosphorus after dissolution test) / Amount of phosphorus before dissolution test × 100

<Fenton test>
Ferrous sulfate (7 hydrate) 0.149 g was dissolved in 1 L of water to prepare a 30 ppm Fe aqueous solution. Fenton reagent was prepared by adding 50 g of 30% hydrogen peroxide solution to 50 ml of 30 ppm Fe aqueous solution, adding water and stirring well to make the total amount 500 ml. The polymer electrolyte membrane 52 mg previously dried for 1 hour at 100 ° C. and then weighed was immersed in 29 ml of Fenton reagent in a reagent bottle and treated at 60 ° C. for 3 hours or 4 hours. The sample was taken out, washed with water, dried at 100 ° C. for 1 hour, and then weighed. When the membrane did not retain its shape, the residue was filtered through a glass filter, dried at 100 ° C. for 1 hour, and then weighed. The residual percentage of the weight after the treatment with respect to the weight before the treatment was determined.

<Transmission electron microscope (TEM) measurement>
The dried polymer electrolyte membrane was embedded in an epoxy resin. The embedded sample was made into an ultrathin section with a microtome, and subjected to carbon deposition to obtain a sample for TEM observation. Observation and photography were performed using a JEM2100 transmission electron microscope manufactured by JEOL Ltd. at an acceleration voltage of 200 kV. In addition, elemental analysis was performed with STEM-EDX.

<X-ray photoelectron spectroscopy (XPS) measurement>
XPS measurement was performed using Shimadzu-Kratos ESCA-3400. MgKα rays were used as the X-ray source, and neutral carbon was shifted to 285 eV.

It shows below about the synthesis | combination of a polymer electrolyte.

<Production Example 1: Synthesis of polymer electrolyte (P1)>
86.90 g (190.9 mmol) of sodium 4,4′-dichlorobenzophenone-3,3-disulfonate, 41.91 g (242.9 mmol) of 2,6-dichlorobenzonitrile (abbreviation: DCBN), 4,4′- Biphenol (abbreviation: BP) 65.14 g (353.6 mmol), 2,2-bis (4-hydroxyphenyl) hexafluoropropane (abbreviation: 6F-BisA) 26.81 g (80.2 mmol), potassium carbonate 65.95 g (477.2 mmol), 500 ml of NMP, and 100 ml of toluene were placed in a 1000 ml branch flask equipped with a nitrogen introduction tube, a stirring blade, a Dean-Stark trap, and a thermometer, and heated in a nitrogen stream while stirring in an oil bath. After dehydration by azeotropy with toluene at 140 ° C., all toluene was distilled off. Then, it heated up at 200 degreeC and heated for 5 hours. The reaction solution was cooled to room temperature, poured into 3000 ml of pure water to solidify the oligomer, and further washed 5 times with pure water to remove NMP and inorganic salts. After separation by filtration, the polymer electrolyte (P1) of a random copolymer was obtained by drying under reduced pressure at 120 ° C. for 16 hours. Hereinafter, the polymer electrolyte is abbreviated as (P1). The chemical structure of P1 is shown below. The logarithmic viscosity of P1 was 1.2 dL / g.

[In the above formula, X represents Na ion or K ion. ]

<Production Example 2: Synthesis of hydrophobic oligomer>
2,6-dichlorobenzonitrile (abbreviation: DCBN) 30.00 g (173.9 mmol), 4,4′-biphenol (abbreviation: BP) 33.75 g (181.1 mmol), potassium carbonate 27.54 g (199.2 mmol) ), 440 ml of NMP was placed in a 1000 ml branch flask equipped with a nitrogen introduction tube, a stirring blade, a Dean-Stark trap, and a thermometer, and heated in a nitrogen stream while stirring in an oil bath. The temperature was raised to 200 ° C. and stirred for 4 hours. The reaction solution was cooled to room temperature, poured into 3000 ml of pure water to solidify the oligomer, and further washed with pure water three times to remove NMP and inorganic salts. The oligomer washed with water was separated by filtration and then dried under reduced pressure at 120 ° C. for 16 hours to obtain a hydrophobic oligomer. ^The number average molecular weight determined by ¹ H-NMR measurement was 6840.

<Production Example 3: Synthesis of hydrophilic oligomer>
4,4′-dichlorodiphenylsulfone-3,3′-sodium disulfonate (abbreviation: S-DCDPS) 250.0 g (508.9 mmol), BP 103.5 g (555.2 mmol), potassium carbonate 84.40 g (610. 7 mmol), 700 ml of NMP, and 150 ml of toluene were placed in a 2000 ml branch flask equipped with a nitrogen introduction tube, a stirring blade, a Dean-Stark trap and a thermometer, and heated in a nitrogen stream while stirring in an oil bath. After dehydration by azeotropy with toluene at 140 ° C., all toluene was distilled off. Then, it heated up at 200 degreeC and heated for 16 hours. Subsequently, 500 ml of NMP was added and cooled to room temperature with stirring. The obtained solution was subjected to suction filtration with a 25G2 glass filter, whereby a yellow transparent solution was obtained. The obtained solution was dropped into 3 L of acetone to solidify the oligomer. The oligomer was further washed three times with acetone, then filtered and dried under reduced pressure to obtain a hydrophilic oligomer. ^The number average molecular weight determined by ¹ H-NMR measurement was 6650. The chemical structure of the hydrophilic oligomer is shown below.

[In the above formula, X represents Na ion or K ion. ]

<Production Example 4: Synthesis of polymer electrolyte (P2)>
6.95 g of hydrophilic oligomer, 6.44 g of hydrophobic oligomer, and 110 ml of NMP were placed in a 200 ml branch flask equipped with a nitrogen introduction tube, a stirring blade, a Dean-Stark trap and a thermometer, and placed in an oil bath at 70 ° C. under a nitrogen stream. Stir to dissolve. Thereafter, 0.67 g of decafluorobiphenyl (DFB) and 0.25 g of potassium carbonate were added, heated to 110 ° C., and reacted for 10 hours. The solid content concentration of the reaction solution was 10% by weight. Then, it cooled to room temperature and it was dripped in 1L pure water, and the polymer was solidified. After washing with pure water three times, it was treated at 80 ° C. for 5 hours while immersed in pure water. Further, the polymer from which water was removed was immersed in a mixed solvent of 1000 ml of isopropanol and 500 ml of water at room temperature for 16 hours, and the polymer was taken out and washed. The same operation was performed again. Thereafter, the polymer was filtered off and dried under reduced pressure at 120 ° C. for 12 hours to obtain a polymer electrolyte (P2). The logarithmic viscosity of P2 was 2.2 dL / g. The composition ratio of the hydrophilic segment and the hydrophobic segment determined from ¹ H-NMR was 32/68.

The synthesis of a copolymer of vinylphosphonic acid (VP) and N-isopropylacrylamide (NIPAAm) is shown below.

J. et al. Appl. Poly. sci. , 70 1947 (1998), a random polymer (VP-N) having a unit structure represented by the following was obtained. Analysis of the amount of phosphorus revealed that the amount of phosphorus in this polymer was 0.11 g / g of polymer.

Example 1
P2 was immersed in 2N sulfuric acid overnight to convert the sulfonic acid group to the acid form, washed with pure water to remove free sulfuric acid, and dried under reduced pressure at 110 ° C. for 8 hours. 0.12 g of 2% NMP solution of acetylacetone zirconium (Kishida Chemical Co., Ltd.) was added to 20 g of 12% NMP solution of acid type P2 thus obtained and mixed, and 10% aqueous solution of polyvinylphosphonic acid (abbreviated as PVPA, manufactured by PANCHIM) was added. 6 g was added and mixed. Then, it casted with the thickness of 300 micrometers on the glass plate using the applicator, heated at 100 degreeC for 2 hours, and dried. Thereafter, the glass plate was allowed to cool to near room temperature, and the membrane was peeled off with water attached to the membrane. The peeled membrane was washed with pure water to remove residual NMP, and then air-dried to obtain a polymer electrolyte membrane.

Example 2
A polymer electrolyte membrane was prepared in the same manner as in Example 1 except that P1 was used instead of P2 and the amount of 2% NMP solution of acetylacetone zirconium was 1.2 g.

Example 3
A polymer electrolyte membrane was prepared in the same manner as in Example 1 except that the amount of 2% NMP solution of acetylacetone zirconium was 0.05 g and the amount of 10% aqueous solution of PVPA was 0.3 g.

Example 4
Aside from using 0.2 g of 3% NMP solution of acetylacetonezirconium instead of 0.2 g of 2% NMP solution of acetylacetonezirconium and 1.5 g of 20% aqueous solution of PVPA instead of 0.3 g of 10% aqueous solution of PVPA A polymer electrolyte membrane was prepared in the same manner as in Example 1.

Example 5
P2 was immersed in 2N sulfuric acid overnight to convert the sulfonic acid group to the acid form, washed with pure water to remove free sulfuric acid, and dried under reduced pressure at 110 ° C. for 8 hours. 1.4 g of 10% aqueous solution of PVPA was added to and mixed with 20 g of 12% NMP solution of acid type P2 thus obtained, and 1.6 g of 2% NMP solution of acetylacetone zirconium was added and mixed. Then, it casted with the thickness of 300 micrometers on the glass plate using the applicator, heated at 100 degreeC for 2 hours, and dried. Thereafter, the glass plate was allowed to cool to near room temperature, and the membrane was peeled off with water attached to the membrane. The peeled membrane was washed with pure water to remove residual NMP, and then air-dried to obtain a polymer electrolyte membrane.

Example 6
20 mg of acetylacetone zirconium was added to 20 g of 12% NMP solution of P2, and mixed until acetylacetonezirconium was dissolved. Then, it casted with the thickness of 300 micrometers on the glass plate using the applicator, heated at 100 degreeC for 2 hours, and dried. Thereafter, the glass plate was allowed to cool to near room temperature, and the membrane was peeled off with water attached to the membrane. Thereafter, the membrane was immersed and washed in pure water, immersed in 2N sulfuric acid for 1 hour to convert the sulfonic acid group to the acid form, washed with pure water to remove free sulfuric acid, and air-dried. This membrane was immersed in an excess amount of a 10% aqueous solution of PVPA and heated to reflux for 1 hour. After the treatment, the membrane was washed with water at room temperature and air-dried to obtain a polymer electrolyte membrane.

Example 7
Zr of 85% zirconium (IV) butoxide, 1-butanol solution (manufactured by Wako Pure Chemical Industries), acetylacetone (manufactured by Tokyo Chemical Industry) and acetic acid (manufactured by Nacalai Tesque) instead of 0.2 g of 2% NMP solution of acetylacetone zirconium A polymer electrolyte membrane was prepared in the same manner as in Example 1 except that 0.03 g of a 1: 2: 1 molar ratio of acetylacetone and acetic acid was used and the amount of 10% aqueous solution of PVPA was 0.6 g. .

Example 8
A polymer electrolyte membrane was obtained in the same manner as in Example 1 except that 0.6 g of a 10% methanol solution of VP-N was used instead of PVPA.

Example 9
A polymer electrolyte membrane was prepared in the same manner as in Example 3 except that 0.15 g of a 2% NMP solution of acetylacetone cerium (III) (dihydrate) (manufactured by Kishida Chemical) was used instead of acetylacetone zirconium.

Comparative Example 1
20 g of 12% NMP solution of P1 was cast on a glass plate with a thickness of 300 μm using an applicator, heated at 100 ° C. for 2 hours, and dried. Thereafter, the glass plate was allowed to cool to near room temperature, and the membrane was peeled off with water attached to the membrane. The peeled membrane is immersed in pure water, and then immersed in 1N sulfuric acid for 1 hour to convert the sulfonic acid group to an acid form, washed with pure water to remove free sulfuric acid, and air-dried to form a polymer electrolyte membrane. Obtained.

Comparative Example 2
A polymer electrolyte membrane was prepared in the same manner as in Comparative Example 1 except that P2 was used instead of P1.

Comparative Example 3
A polymer electrolyte membrane was prepared in the same manner as in Example 3 except that acetylacetone zirconium was not added.

Comparative Example 4
20 g of a 12% NMP solution of P2 and 0.6 g of a 5% NMP / water = 15/85 (wt / wt) solution of PVPA were mixed. Then, it casted with the thickness of 300 micrometers on the glass plate using the applicator, heated at 100 degreeC for 2 hours, and dried. Thereafter, the glass plate was allowed to cool to near room temperature, and the membrane was peeled off with water attached to the membrane. The peeled film was immersed in pure water and then immersed in a 0.015 wt% aqueous solution of ZrOCl ₂ .8H ₂ O overnight. Thereafter, the membrane is immersed in pure water for washing, then immersed in 2N sulfuric acid for 1 hour to convert the sulfonic acid group to an acid form, washed with pure water to remove free sulfuric acid, and air-dried to form a polymer electrolyte. A membrane was obtained.

Comparative Example 5
0.4 g of the proton exchange membrane obtained in Comparative Example 2 was immersed in 100 ml of a 4 wt% aqueous solution of ZrOCl ₂ .8H ₂ O and heated to reflux for 2 hours. Thereafter, the membrane was taken out and immersed in a 50% aqueous solution of nitrilotris (methylenephosphonic acid) (Chillest Co., Ltd.) overnight. The membrane was washed with pure water to remove free acid, and air-dried to obtain a proton exchange membrane.

  Table 1 shows the proton conductivity of the polymer electrolyte membranes obtained in Examples and Comparative Examples.

In Examples 1 to 9 in which the phosphorus-containing polymer compound and the metal element were uniformly dispersed in the film with a size of 0.5 μm or less, the proton conductivity was higher than those in Comparative Examples 1 and 2 in which no additive was added. Indicated.

The polymer electrolyte membranes obtained in the examples and comparative examples were subjected to TEM and XPS measurements in order to evaluate the dispersibility of the additives. An example of a TEM photograph is shown in FIG. When STEM-EDX analysis was performed, in Example 1, P and Zr were detected from the part which looks black. In Comparative Example 4, P was detected from a black portion of the film, and P and Zr were detected from a black surface portion of the film surface. The size of the composition containing a phosphorus element and a metal element was determined from the size of the black portion of the TEM photograph.
Add a film containing a phosphorus-containing polymer compound and a metal element, the composition containing the phosphorus element and the metal element having a size of 0.5 μm or less, and having no layer containing the phosphorus element and the metal element on the film surface. It was determined that the agent was uniformly dispersed.

Table 2 shows the size of the composition containing phosphorus element and metal element determined from the TEM photograph. In Comparative Examples 3 and 4, since the metal element was not detected from the black part in the film, the size of the composition containing the phosphorus element and not containing the metal element is shown. In Comparative Example 4, it is presumed that the amount of Zr element in the film was below the detection limit because of the large amount of Zr element on the film surface.
Table 2 shows the analysis results of the element amounts on the film surface obtained by XPS measurement. The ratio with respect to the total amount of metal elements on the film surface was obtained from the following formula. The XPS detection range was calculated as 0.0075 μm.
Ratio to the total amount of metal elements on the film surface = [{Zr amount on the film surface (Atom%) × 0.0075 (μm) / film thickness (μm)} / Zr amount on the entire film (Atom%)] × 100

In Comparative Examples 3 and 4, the black portion in the TEM photograph has a string-like shape, and a clear length could not be determined, so the width of the black portion is shown.
In Examples 1 to 9, the size of the composition containing the phosphorus element and the metal element was 0.5 μm or less, and no surface layer containing the additive as seen in Comparative Example 4 was found. In XPS analysis, too much Zr element was present on the film surface in Comparative Example 4, but in Examples 1 to 9, the Zr element was below the detection limit, and was a reasonable value when Zr was uniformly dispersed throughout the film. there were.

  A Fenton test was performed on the polymer electrolyte membranes obtained in Examples and Comparative Examples. The results are shown in Table 3.

The polymer electrolyte membrane of the random polymer of Comparative Example 1 was in a very fragile state in 3 hours, and almost no shape was retained in 4 hours. The polymer electrolyte membrane of the block copolymer polymer of Comparative Example 2 was in a state where the hydrophilic segment was completely removed in 4 hours and only the hydrophobic portion remained. The polymer electrolyte membranes to which the phosphorus-containing compounds of Examples 1 to 9 and Comparative Examples 3 to 5 were added showed little change in weight, and it was confirmed that the Fenton resistance was increased by the addition of the phosphorus-containing compound.

  The polymer electrolyte membranes obtained in Examples and Comparative Examples were subjected to a phosphorus-containing compound elution test and a membrane Fenton test after the elution test. The results are shown in Table 4.

Phosphorus elution was observed in Comparative Example 3 in which only the phosphorus-containing polymer compound was added by immersion in water at 80 ° C. for 48 hours, but Examples 1 to 9 in which the phosphorus-containing polymer compound and the metal element were added. In Comparative Example 4, elution of phosphorus was suppressed. In Comparative Example 5 in which a low molecular weight phosphorus-containing compound and a metal element were added, suppression of phosphorus elution was insufficient.
When the Fenton test of the film after the dissolution test was performed, Examples 1 to 9 in which the phosphorus-containing polymer compound and the metal element were added were Comparative Example 3 in which the metal element was not added and Comparative Example in which suppression of dissolution was insufficient. It is considered that Fenton resistance higher than 5 is exhibited, and long-term high oxidation resistance can be obtained by suppressing elution of the phosphorus-containing polymer compound by addition of a metal element.

  A power generation test was performed on the polymer electrolyte membranes obtained in the examples and comparative examples. The results are shown in Table 5.

The power was higher in Example 1 than in Comparative Example 2 and showed high battery performance.

From the above results, it has been clarified that the oxidation resistance is improved by mixing the phosphorus-containing polymer compound with the polymer electrolyte. It has also been clarified that the elution of the phosphorus-containing polymer compound is suppressed by adding a metal element in addition to the phosphorus-containing polymer compound. Furthermore, the proton conductivity was improved by uniformly dispersing the phosphorus-containing polymer compound and the metal element in a size of 0.5 μm or less. From the above, it is possible to obtain a solid polymer electrolyte membrane with improved long-term oxidation resistance and improved proton conductivity.

The present invention relates to an excellent polymer electrolyte membrane that can improve oxidation resistance and proton conductivity without causing elution of additive components, a membrane / electrode assembly using the polymer electrolyte membrane, and a fuel It provides batteries and contributes to the industry.

Claims (9)

A polymer electrolyte membrane comprising a solid polymer electrolyte composition containing 90 to 99.95 parts by mass of an aromatic hydrocarbon polymer electrolyte, 0.05 to 10 parts by mass of a phosphorus-containing polymer compound, and 10 to 5000 ppm of a metal element. Te, viewed contains a phosphorus element and the metal element present in the polymer electrolyte membrane, a non-water-soluble or polymer electrolyte membrane composition is poorly soluble are uniformly dispersed in the following sizes 0.5 [mu] m. The polymer electrolyte membrane according to claim 1, wherein the metal element is one or more metal elements selected from the group consisting of alkaline earth metals, transition metals, and rare earth elements. Metal element content in the film surface 5~10nm of the polymer electrolyte membrane is 10% or less of the total amount, film thickness of 5 to 30 [mu] m, according to claim 1 or 2 Polymer electrolyte membrane. Of claims 1 to 3 is film formation from a solution containing a mixed solvent of an aprotic polar solvent or an aprotic polar solvent and water or an alcohol to dissolve the polymer electrolyte and a metal alkoxide or metal chelate compound and the polymer electrolyte The polymer electrolyte membrane according to any one of the above. It is formed from a polyelectrolyte and a metal alkoxide or metal chelate compound, a phosphorus-containing polymer compound and a solution containing an aprotic polar solvent or a mixed solvent of an aprotic polar solvent and water or an alcohol. The polymer electrolyte membrane according to any one of claims 1 to 3 . 6. The polymer electrolyte membrane according to claim 1 , wherein the phosphorus-containing polymer compound is polyvinylphosphonic acid. According to claim 1, wherein the metallic element is Mg, Ca, Co, Ni, Zn, Sr, Zr, Ba, characterized in that one or more metal elements selected from the group consisting of Ce Polymer electrolyte membrane. A membrane / electrode assembly using the polymer electrolyte membrane according to claim 1 . A fuel cell using the membrane / electrode assembly according to claim 8 .