JP2007157455A - Polymer electrolyte, polymer electrolyte membrane, membrane-electrode assembly, and solid polymer electrolyte fuel cell - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a polymer electrolyte cost-effective, eco-friendly, excellent in moldability, and excellent in heat resistance. <P>SOLUTION: The polymer electrolyte is made of a block copolymer which has a polymer block A and a flexible polymer block B as constituents where the polymer block A has an ion conductive group and a structural unit originated from a styrene derivative expressed by a formula I, where R<SP>1</SP>is a cycloaliphatic hydrocarbon radical having a polycyclic structure, and R<SP>2</SP>is a hydrogen atom, an alkyl group, or an aryl group. A polymer electrolyte membrane uses the polymer electrolyte. A membrane-electrode assembly and a polymer electrolyte fuel cell use them. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

  The present invention relates to a polymer electrolyte excellent in heat resistance, a polymer electrolyte membrane comprising the polymer electrolyte, a membrane-electrode assembly and a solid polymer fuel cell using the electrolyte membrane.

  In recent years, fuel cell technology has been counted as one of the pillars of these new energy technologies as a fundamental solution to energy and environmental problems, and as a central energy conversion system in the future hydrogen energy era. In particular, polymer electrolyte fuel cells (PEFCs) are used for stationary power sources that use both electric power and heat, as well as power sources for electric vehicles and portable devices, from the viewpoint of miniaturization and weight reduction. Application to other power supply devices is under consideration.

  A polymer electrolyte fuel cell is generally configured as follows. First, a catalyst layer containing carbon powder carrying a white metal catalyst and an ion conductive binder made of a polymer electrolyte is formed on both sides of a polymer electrolyte membrane having proton conductivity. A gas diffusion layer, which is a porous material through which fuel gas and oxidant gas are passed, is formed outside each catalyst layer. Carbon paper, carbon cloth, or the like is used as the gas diffusion layer. A structure in which the catalyst layer and the gas diffusion layer are integrated is called a gas diffusion electrode, and a structure in which a pair of gas diffusion electrodes is bonded to the electrolyte membrane so that the catalyst layer faces the electrolyte membrane is a membrane-electrode assembly ( MEA (Membrane Electrode Assembly). On both sides of this membrane-electrode assembly, separators having electrical conductivity and airtightness are disposed. A gas flow path for supplying a fuel gas or an oxidant gas (for example, air) to the electrode surface is formed in a contact portion of the membrane-electrode assembly and the separator or in the separator. Electric power is generated by supplying a fuel gas such as hydrogen or methanol to one electrode (fuel electrode) and an oxidant gas containing oxygen such as air to the other electrode (oxygen electrode). That is, at the fuel electrode, the fuel is ionized to produce protons and electrons, the protons pass through the electrolyte membrane, the electrons travel through an external electric circuit formed by connecting both electrodes, and are sent to the oxygen electrode, Water is produced by the reaction. In this way, the chemical energy of the fuel can be directly converted into electric energy and taken out.

  In order to put the polymer electrolyte fuel cell (PEFC), which is expected as a dream next-generation energy to replace the internal combustion engine for automobiles, to practical use and diffusion, (1) improvement of electrode activity, (2) in reformed hydrogen gas It is important to set the operating temperature (currently 60 to 80 ° C.) to 120 ° C. or higher from the viewpoint of poisoning of the anode catalyst by CO contained in (3), utilization of waste heat by heat exchange, and the like. However, perfluoro-based electrolyte membranes typified by DuPont Nafion are not capable of withstanding high-temperature operation because proton conductivity and membrane strength are significantly reduced at temperatures of 100 ° C. or higher.

Aiming at development of heat-resistant polymer electrolyte membranes that can withstand stable operation at high temperatures of 100 ° C or higher, membranes based on heat-resistant polymers and perfluoro-based polymer electrolyte membranes with improved softening temperature of the main chain Is being considered. However, in general, perfluoro-based polymer electrolyte membranes are expensive and difficult to spread to general consumers. In addition, since a large amount of halogen (fluorine) is contained in the raw material resin, future disposal problems or It has been pointed out that hydrogen fluoride may be released into the atmosphere. On the other hand, polymer electrolyte membranes based on heat-resistant polymers, so-called engineering plastics (hereinafter abbreviated as engineering plastics) are hydrocarbon-based polymer electrolyte membranes that do not substantially contain halogen, and are perfluoro-based polymer electrolytes. It is said that the heat resistance is higher than that of the film. For example, an example in which polyether ether ketone (PEEK), which is a heat-resistant aromatic polymer, is sulfonated has been reported (Patent Document 1). However, polymer electrolyte membranes based on engineering plastics are generally known to be inferior in chemical stability (radical resistance), and proton conductivity and mechanical properties are inferior to those of perfluoropolymer electrolyte membranes. It is said to be inferior.

  Thus, in PEFC for automobiles, a novel polymer electrolyte membrane with high heat resistance that is stably driven at a high temperature of 100 ° C. or higher is required.

  Several efforts have already been made for the development of ion conductive polymers based on non-fluorinated polymers. For example, there is an example in which a polystyrene sulfonic acid polymer electrolyte membrane is used in a solid polymer fuel cell developed by General Electric in the United States in the 1950s. However, since there was not sufficient stability, sufficient battery life could not be obtained.

  On the other hand, as a polymer electrolyte membrane for a polymer electrolyte fuel cell, an example in which ion conductivity necessary for an electrolyte membrane is expressed using an ion channel formed by a specific constituent unit (block) in a block polymer has been reported. Has been. Specifically, research examples of hydrocarbon polymer electrolyte membranes in which styrene sites of styrene block polymers are sulfonated are known (Patent Documents 2 to 5), and can be used as electrolyte membranes for fuel cells. Has been reported. In particular, electrolyte membranes based on thermoplastic elastomers represented by SEBS (styrene-ethylene / butene-styrene triblock polymer) are (1) low cost, (2) non-halogenous, and (3) thermoplastic. It is easy to form a film, and (4) it has a flexible and elastic property so that it has a high shape retention capability against repeated humidification / drying, etc., and the conventional fluoropolymer electrolyte membrane or engineering plastic polymer electrolyte membrane Is a unique aromatic hydrocarbon polymer electrolyte membrane with different characteristics. However, since all the base polymers studied in past reports are block polymers having polystyrene units as hard segments, higher order is required in the temperature region above the glass transition temperature of the hard segments (specifically, about 100 ° C). Since the structure, that is, the ion channel structure is not maintained, proton conductivity and mechanical strength are greatly reduced. This is the same phenomenon that the performance of Nafion is greatly reduced above the glass transition temperature.

Thus, the present situation is that no improved polymer electrolyte membrane for a polymer electrolyte fuel cell, which is economical and has high heat resistance, has been proposed.
JP-A-6-93114 Special Table 2000-503788 US Pat. No. 5,468,574 JP 2003-142125 A Japanese Patent Laid-Open No. 2001-210336 “Synthesis”, 1998, No. 2, pages 148-152.

  An object of the present invention is a polymer electrolyte that is economical, environmentally friendly, excellent in moldability, and excellent in heat resistance, a polymer electrolyte membrane comprising the polymer electrolyte, and a membrane using the electrolyte membrane- An electrode assembly and a polymer electrolyte fuel cell are provided.

As a result of intensive research to solve the above-mentioned problems, the present inventors have repeatedly repeated a unit derived from a specific styrene derivative having a benzene ring having a substituent composed of an alicyclic hydrocarbon group having a polycyclic structure. A polymer electrolyte comprising a polymer block (A) as a unit and a flexible polymer block (B) as a constituent component and a block copolymer having an ion conductive group in the polymer block (A) The inventors have found that the above object is satisfied and completed the present invention.
That is, the present invention provides the following general formula (I):

(In the formula, R ¹ represents an alicyclic hydrocarbon group having a polycyclic structure, and R ² represents a hydrogen atom, an alkyl group having 1 to 10 carbon atoms, or an aryl group.)
A block having a polymer block (A) having a structural unit derived from a styrene derivative represented by the formula (B) and a flexible polymer block (B) and having an ion conductive group in the polymer block (A) The present invention relates to a polymer electrolyte made of a copolymer.

In the block copolymer, the polymer block (A) and the polymer block (B) undergo microphase separation, and the polymer block (A) and the polymer block (B) are aggregated. In addition, since the polymer block (A) has an ion conductive group, an ion channel is formed by the assembly of the polymer blocks (A), and it serves as a passage for ions and functions as a polymer electrolyte. Further, as a repeating unit constituting the polymer block (A), by selecting a specific styrene derivative having a substituent composed of an alicyclic hydrocarbon group having a polycyclic structure in the benzene ring, the polymer block ( The glass transition temperature of A) is significantly increased, and as a result, the heat resistance of the entire polymer electrolyte is greatly improved.
The present invention also relates to a membrane containing the polymer electrolyte, a membrane-electrode assembly for a polymer electrolyte fuel cell using the membrane, and a fuel cell.

  The polymer electrolyte of the present invention is economical and environmentally friendly, has high heat resistance, and sufficiently functions even under high temperature conditions. The membrane containing the polymer electrolyte and the membrane-electrode assembly using the membrane are solid polymer fuel cells, particularly solid polymer types for automobiles that are required to operate stably under high temperature conditions. It is suitably used for a fuel cell.

The present invention will be described in detail below. The block copolymer constituting the polymer electrolyte of the present invention is represented by the following general formula (hereinafter, referred to as “styrene derivative (I)”) represented by the general formula (I): The polymer block (A) has a structural unit represented by I ′) (hereinafter sometimes referred to as “structural unit (I ′)”). Even if the polymer block (A) contains only a single structural unit (I ′), two or more structural units (I ′) differing in any of the substitution positions of R ¹ , R ² and R ¹ May be contained. When two or more kinds of structural units (I ′) are contained, the copolymerization form of the styrene derivative (I) may be random copolymerization, block copolymerization, graft copolymerization, or tapered copolymerization.

(In the formula, R ¹ represents an alicyclic hydrocarbon group having a polycyclic structure, and R ² represents a hydrogen atom, an alkyl group having 1 to 10 carbon atoms, or an aryl group.)

In the styrenic derivative (I), and hence the structural unit (I ′), R ¹ is an alicyclic hydrocarbon group having a polycyclic structure. Here, the “alicyclic hydrocarbon group having a polycyclic structure” means a hydrocarbon group having two or more aliphatic rings (alicyclic rings). The alicyclic hydrocarbon group having a polycyclic structure (hereinafter sometimes referred to as “polyalicyclic hydrocarbon group”) R ¹ is a bridged alicyclic hydrocarbon group, that is, two adjacent alicyclic rings. A hydrocarbon group that shares the above carbon atoms with each other is preferable from the viewpoint of improving the heat resistance of the block copolymer of the present invention. The polyalicyclic hydrocarbon group R ¹ may optionally have an aliphatic unsaturated bond in one or more of the two or more alicyclic rings constituting R ¹ . However, it is necessary that the aliphatic unsaturated bond present in the alicyclic ring does not participate in the polymerization or has a lower polymerizability than the vinyl bond in the styrene derivative (I). Otherwise, smooth polymerization of the styrene derivative (I) is hindered, and it becomes difficult to smoothly obtain the block copolymer having the structural unit (I ′).

Specific examples of the polyalicyclic hydrocarbon group R ¹ include an adamantyl group (tricyclo [3.3.1.1 ^3,7 ] decyl group), a biadamantyl group, a norbornyl group, an isobornyl group, a bicyclononyl group, a bicyclo group. Examples include [2.1.0] pentyl group, bicyclo [3.2.1] octyl group, tricyclo [2.2.1.0 ^2,6 ] heptyl group. These polyalicyclic hydrocarbon groups may be optionally substituted with an alkyl group, a halogen, an alkoxyl group or the like.

The bonding position of the polyalicyclic hydrocarbon group R ^{1 in} the styrene derivative (I) at the benzene ring is ortho to the bonding site of the vinyl bond [—C (R ² ) ═CH ₂ ] in the benzene ring, Either the meta position or the para position may be used, and among them, the polyalicyclic hydrocarbon group R ¹ may be bonded to the para position from the viewpoint of polymerization reactivity of the styrene derivative (I). preferable.

In the styrene derivative (I) represented by the above general formula (I), and thus the structural unit (I ′) represented by the above general formula (I ′), R ² is a hydrogen atom, having 1 to 10 carbon atoms. Either an alkyl group or an aryl group may be used. When R ² is an alkyl group having 1 to 10 carbon atoms, it may be linear or branched, specifically, methyl group, ethyl group, propyl group, butyl group, pentyl group, hexyl. Group, straight chain alkyl group such as heptyl group, octyl group, nonyl group, decyl group, isopropyl group, isobutyl group, sec-butyl group, tert-butyl group, isopentyl group, neopentyl group, tert-pentyl group, 1- Examples thereof include branched alkyl groups such as methylheptyl group.
Specific examples of R ² being an aryl group include a phenyl group and a naphthyl group. These aryl groups are alkyl groups having 1 to 4 carbon atoms (methyl group, ethyl group, etc.). May have one or more substituents such as a halogen atom and an alkoxyl group having 1 to 4 carbon atoms (methoxy group, ethoxy group, etc.).

Among the above, R ² is preferably a hydrogen atom, an alkyl group having 1 to 4 carbon atoms, or an aryl group from the viewpoints of ease of production of the styrene derivative (I) and polymerization reactivity. Further, when the block copolymer of the present invention is used as a polymer electrolyte membrane for a polymer electrolyte fuel cell or a membrane-electrode assembly, chemical stability, particularly radical resistance, may be required. In such a case, R ² is more preferably an alkyl group having 1 to 4 carbon atoms or an aryl group, and R ² is more preferably a methyl group in consideration of ease of production and polymerization reactivity.

Specific examples of the styrene derivative (I) that can be preferably used for the production of the block copolymer of the present invention include styrene derivatives represented by the following chemical formula. In the following chemical formula, R ² has the same meaning as in general formula (I).

Among the styrene derivatives described above, 1- (4-vinylphenyl) adamantane [also known as 4- (1-adamantyl) styrene] represented by the above chemical formula (Ia) in which R ¹ is an adamantyl group, and R ^One or both of 3- (4-vinylphenyl) -1,1′-biadamantane represented by the above chemical formula (Ib), wherein ¹ is a biadamantyl group, particularly 1- (4-vinylphenyl) adamantane The polymer of the present invention having a structural unit derived from is preferable because of excellent heat resistance and easy monomer production.

The polymer block (A) may contain one or more other monomer units different from the structural unit (I ′) within a range not impairing the effects of the present invention. Such other monomers include, for example, aromatic vinyl compounds different from styrene derivatives (I), conjugated dienes having 4 to 8 carbon atoms, alkenes having 2 to 8 carbon atoms, (meth) acrylic acid or esters thereof, fats A vinyl ester of an aromatic carboxylic acid, an alkyl vinyl ether, an unsaturated halogenated hydrocarbon, an unsaturated aliphatic nitrile, a (meth) acrylamide compound, an unsaturated dicarboxylic acid derivative, and the like. Among these, an aromatic vinyl compound different from the styrene derivative (I) is particularly preferable.
The copolymerization form of the styrene derivative (I) and the other monomer needs to be random copolymerization.

The aromatic vinyl compound different from the styrene derivative (I) is styrene, α-methylstyrene, o-methylstyrene, m-methylstyrene, p-methylstyrene, 2,4-dimethylstyrene,. -P-methylstyrene, o-methoxystyrene, m-methoxystyrene, p-methoxystyrene, 1,1-diphenylethylene, vinylnaphthalene, vinylanthracene, 2-vinylpyridine, 4-vinylpyridine, etc .; (meth) acrylic acid Or as its ester, acrylic acid, methyl acrylate, ethyl acrylate, butyl acrylate, adamantyl acrylate, methacrylic acid, methyl methacrylate, ethyl methacrylate, butyl methacrylate, 2-ethylhexyl methacrylate, 2-hydroxy methacrylate ethyl, Adamantyl tacrylate, etc .; vinyl acetate of aliphatic carboxylic acid, vinyl acetate, vinyl propionate, vinyl butyrate, vinyl pivalate, etc .; alkyl vinyl ether, methyl vinyl ether, isobutyl vinyl ether, etc .; unsaturated halogenated hydrocarbon, vinyl chloride , Vinylidene chloride, vinyl fluoride, vinylidene fluoride, tetrafluoroethylene, etc .; unsaturated aliphatic nitriles such as acrylonitrile, methacrylonitrile, etc .; (meth) acrylamide compounds as acrylamide, N-methylacrylamide, N, N- Dimethylacrylamide, N-isopropylacrylamide, N, N-diisopropylacrylamide, methacrylamide, N-methylmethacrylamide, N, N-dimethylmethacrylamide N-isopropyl methacrylamide, N, N-diisopropyl methacrylamide, etc .; Examples of unsaturated dicarboxylic acid derivatives include maleic anhydride and diethyl fumarate.
In the above, specific examples of the conjugated diene having 4 to 8 carbon atoms and the alkene having 2 to 8 carbon atoms can be the same as those exemplified in the description of the polymer block (B) described later.

  When the polymer block (A) has a structural unit derived from another monomer together with the structural unit (I ′), the other monomer forming the polymer block (A) is a styrene derivative (I). It is preferable from the point of the ease of copolymerization with a styrene derivative (I) that it is 1 type (s) or 2 or more types of aromatic vinyl compounds other than). In particular, when the structural unit (I ′) is a 1- (4-vinylphenyl) adamantane unit and / or a 3- (4-vinylphenyl) -1,1′-biadamantane unit, the other monomer unit is More preferred is a styrene unit.

  The proportion of the structural unit (I ′) in the polymer block (A) is preferably 10 mol% or more from the viewpoint of imparting sufficient heat resistance to the finally obtained polymer electrolyte, and is 20 mol%. More preferably, it is more preferably 30 mol% or more, and on the other hand, it is preferably 90 mol% or less because of the ease of introduction of the ion conductive group.

  The molecular weight of the polymer block (A) is appropriately selected depending on the properties of the polymer electrolyte, required performance, other polymer components, etc., but the number average molecular weight in terms of polystyrene is usually from 100 to 1,000,000. It is preferable to select between, and it is more preferable to select between 1,000 and 100,000.

  In the block copolymer of the present invention, the ratio of the polymer block (A) is preferably 10% by mass or more, more preferably 13 to 50% by mass based on the mass of the block copolymer. . Further, the ratio of the structural unit (I ′) to the total mass of the block copolymer is preferably 5% by mass or more, more preferably 10% by mass or more, and 15 to 50% by mass. Further preferred. When the proportion of the structural unit (I ′) is less than 10% by mass, the effect of improving the heat resistance by the structural unit (I ′) is hardly exhibited.

  The block copolymer used in the polymer electrolyte membrane of the present invention has a flexible polymer block (B) in addition to the polymer block (A). The polymer block (A) and the polymer block (B) undergo a microphase separation, and the polymer block (A) and the polymer block (B) have a property of gathering together, and the polymer block (A ) Has an ion conductive group, so that an ion channel as a continuous phase is formed by the assembly of the polymer blocks (A) and becomes a passage for protons. By having such a polymer block (B), the block copolymer becomes elastic and flexible as a whole, and formability (assembly property, bondability) in the production of membrane-electrode assemblies and polymer electrolyte fuel cells. , Tightenability, etc.). The flexible polymer block (B) here is a so-called rubber-like polymer block having a glass transition point or softening point of 50 ° C. or lower, preferably 20 ° C. or lower, more preferably 10 ° C. or lower.

  Monomers that can constitute the repeating unit constituting the flexible polymer block (B) include alkenes having 2 to 8 carbon atoms, cycloalkenes having 5 to 8 carbon atoms, and vinylcycloalkenes having 7 to 10 carbon atoms. , A conjugated diene having 4 to 8 carbon atoms, a conjugated cycloalkadiene having 5 to 8 carbon atoms, and a vinyl cycloalkene having 7 to 10 carbon atoms in which part or all of the carbon-carbon double bond of the cycloalkene moiety has been hydrogenated. , Conjugated cycloalkadienes having 5 to 8 carbon atoms in which up to 50% of carbon-carbon double bonds are hydrogenated, (meth) acrylic acid esters, vinyl esters, vinyl ethers, and the like. Two or more types can be used in combination. The form in the case of polymerizing (copolymerizing) two or more types may be random copolymerization, block copolymerization, graft copolymerization, or tapered copolymerization. Further, when the monomer to be used for (co) polymerization has two carbon-carbon double bonds, any of them may be used for the polymerization, and in the case of a conjugated diene, it is a 1,2-bond. 1,4-bonds may be used, and the ratio of 1,2-bonds to 1,4-bonds is not particularly limited.

When the repeating unit constituting the polymer block (B) has a carbon-carbon double bond as in the case of a vinylcycloalkene unit, a conjugated diene unit, or a conjugated cycloalkadiene unit, the present invention From the standpoints of improving the power generation performance and heat deterioration resistance of the membrane-electrode assembly using the polymer electrolyte, and the membrane-electrode assembly using the membrane, more than 30 mol% of the carbon-carbon double bond is hydrogenated. More preferably, 50 mol% or more is hydrogenated, and 80 mol% or more is more preferably hydrogenated. The hydrogenation rate of the carbon-carbon double bond can be calculated by a commonly used method, for example, iodine value measurement method, ¹ H-NMR measurement or the like.

  The polymer block (B) is an alkene having 2 to 8 carbon atoms from the viewpoint of giving the resulting block copolymer elasticity and, in turn, good moldability in the production of a membrane-electrode assembly and a polymer electrolyte fuel cell. Unit, cycloalkene unit having 5 to 8 carbon atoms, vinylcycloalkene unit having 7 to 10 carbon atoms, conjugated diene unit having 4 to 8 carbon atoms, conjugated cycloalkadiene unit having 5 to 8 carbon atoms, carbon-carbon double 7 to 10 carbon cycloalkene units having some or all of the hydrogenated hydrogen atoms, 4 to 8 carbon conjugated diene units having some or all of the carbon-carbon double bonds hydrogenated, and carbon -A polymer block comprising at least one repeating unit selected from conjugated cycloalkadiene units having 5 to 8 carbon atoms in which some or all of the carbon double bonds are hydrogenated. Preferably, the alkene unit having 2 to 8 carbon atoms, the conjugated diene unit having 4 to 8 carbon atoms, and the conjugated diene unit having 4 to 8 carbon atoms in which some or all of the carbon-carbon double bonds are hydrogenated are selected. More preferably, it is a polymer block composed of at least one type of repeating unit, a conjugated diene unit having 4 to 8 carbon atoms, and 4 to 8 carbon atoms in which some or all of the carbon-carbon double bonds are hydrogenated. It is even more preferable that the polymer block comprises at least one repeating unit selected from conjugated diene units. The most preferred conjugated diene units are 1,3-butadiene units and / or isoprene units.

  As the alkene having 2 to 8 carbon atoms, ethylene, propylene, 1-butene, 2-butene, isobutene, 1-pentene, 2-pentene, 1-hexene, 2-hexene, 1-heptene, 2-heptene, 1 -Octene, 2-octene and the like, and cyclopentene having 5 to 8 carbon atoms include cyclopentene, cyclohexene, cycloheptene and cyclooctene, and vinylcycloalkene having 7 to 10 carbon atoms as vinylcyclopentene, vinylcyclohexene, Examples thereof include vinylcycloheptene and vinylcyclooctene. Examples of the conjugated diene having 4 to 8 carbon atoms include 1,3-butadiene, 1,3-pentadiene, isoprene, 1,3-hexadiene, 2,4-hexadiene, 2 , 3-Dimethyl-1,3-butadiene, 2-ethyl-1,3-butyl Diene, 1,3-heptadiene, 1,4-heptadiene, 3,5-heptadiene and the like, cyclopentadiene, 1,3-cyclohexadiene, and the like as a conjugated cycloalkadiene having 5 to 8 carbon atoms.

  In addition to the above monomers, the polymer block (B) may contain other monomers such as a polymer block as long as it does not impair the purpose of the polymer block (B) to give elasticity to the block copolymer. Aromatic vinyl compounds different from styrene derivatives (I), (meth) acrylic acid or esters thereof, aliphatic carboxylic acid vinyl esters, alkyl vinyl ethers, unsaturated halogens, as mentioned in the description of (A) Hydrocarbons, unsaturated aliphatic nitriles, (meth) acrylamide compounds, unsaturated dicarboxylic acid derivatives and the like may be contained. In this case, the copolymerization form of the monomer and other monomer needs to be random copolymerization. The amount of such other monomer used is preferably less than 50% by weight, more preferably less than 30% by weight, based on the total of the above monomers and other monomers. It is still more preferable that it is less than mass%.

Although the structure of the block copolymer which has a polymer block (A) and a polymer block (B) as a structural component is not specifically limited, ABA type | mold triblock copolymer and ABA are mentioned as an example, for example. Type triblock copolymer and AB type diblock copolymer mixture,
A-A-B-A-B type tetrablock copolymer, (A-B) nX type star copolymer (X represents a coupling agent residue), etc. are mentioned. These block copolymers may be used alone or in combination of two or more.
When the block copolymer of the present invention has two or more polymer blocks (A), they may be the same or different in structure and molecular weight. In addition, when the block copolymer has two or more flexible polymer blocks (B), they may be the same or different in structure and molecular weight.

  The mass ratio of the polymer block (A) and the polymer block (B) is preferably 95: 5 to 5:95, more preferably 90:10 to 10:90, and 50:50 to 10 : 90 is even more preferable. When this mass ratio is 95: 5 to 5:95, it is advantageous for the ion channel formed by the polymer block (A) to become a continuous phase by microphase separation, and practically sufficient ion conduction. In addition, the ratio of the polymer block (B) that is hydrophobic is appropriate, and excellent water resistance is exhibited.

The block copolymer constituting the polymer electrolyte of the present invention may contain another polymer block (C) different from the polymer block (A) and the polymer block (B). Other polymer blocks (C) include polystyrene block, poly p-methyl styrene block, poly p- (t-butyl) styrene block, styrene, p-methyl styrene and p- (t-butyl) of any mutual proportion. ) A copolymer block composed of two or more of styrene is exemplified.
The structure of the block copolymer in this case includes an ABC type triblock copolymer, an ABCA type tetrablock copolymer, and an ABCA type tetrablock copolymer. Examples thereof include C-A-B-A-C type pentablock copolymer.

  When the block copolymer constituting the polymer electrolyte of the present invention contains another polymer block (C), the proportion of the polymer block (C) in the block copolymer is preferably 30% by mass or less. 20 mass% or less is more preferable, and 10 mass% or less is still more preferable.

When the block copolymer of the present invention has a structural unit derived from a conjugated diene and a carbon-carbon unsaturated double bond derived from the conjugated diene is present in the molecule, heat resistance From the standpoint of improving the above, it is preferable that at least a part of the carbon-carbon unsaturated double bond is hydrogenated, and the hydrogenation rate at that time is more preferably 50% or more, and 90% or more. (Hereinafter, hydrogenation may be referred to as “hydrogenation”).
Hydrogenation can be carried out by a generally used method, for example, a method of supplying hydrogen in the presence of a hydrogenation catalyst such as a Ziegler catalyst comprising an alkylaluminum compound and cobalt, nickel, etc., p-toluenesulfonic acid A method of using a compound that generates a diimide such as hydrazide in the system can be employed.

  The number average molecular weight of the block copolymer of the present invention in a state where no ion conductive group is introduced is not particularly limited, but the number average molecular weight in terms of polystyrene is usually preferably 10,000 to 2,000,000. 15,000 to 1,000,000 is more preferable, and 20,000 to 500,000 is even more preferable.

The block copolymer constituting the polymer electrolyte of the present invention needs to have an ion conductive group in the polymer block (A). Examples of ions in the present invention when referring to ionic conductivity include protons. The ion conductive group is not particularly limited as long as the membrane-electrode assembly produced using the polymer electrolyte can express sufficient ion conductivity, but among them -SO ₃ M or -PO. A sulfonic acid group, a phosphonic acid group or a salt thereof represented by ₃ HM (wherein M represents a hydrogen atom, an ammonium ion or an alkali metal ion) is preferably used. As the ion conductive group, a carboxyl group or an ammonium salt or alkali metal salt thereof can also be used. The introduction position of the ion conductive group is the polymer block (A) because it is particularly effective for improving the radical resistance of the entire block copolymer.

There are no particular restrictions on the position at which the ion conductive group is introduced into the polymer block (A). Even if it is introduced into the structural unit (I ′), other monomer units such as styrene derivatives (I ) May be introduced into a unit composed of an aromatic vinyl compound different from the above.
The amount of ion-conducting group introduced is appropriately selected depending on the required performance of the resulting block copolymer, etc., but exhibits sufficient ion conductivity for use as a polymer electrolyte membrane for a polymer electrolyte fuel cell. In general, the amount is preferably such that the ion exchange capacity of the block copolymer is 0.30 meq / g or more, more preferably 0.50 meq / g or more. . The upper limit of the ion exchange capacity of the block copolymer is preferably 3.0 meq / g or less because if the ion exchange capacity is too large, the hydrophilicity tends to increase and the water resistance becomes insufficient.

  In view of heat resistance, the content of the structural unit (I ′) in the polymer electrolyte of the present invention is preferably 5 mol% or more, more preferably 10 mol% or more, and 20 mol% or more. Even more preferably.

  The production method of the block copolymer used in the present invention is roughly classified into the following two methods. That is, (1) First, a method of producing a block copolymer having no ion conductive group and then binding the ion conductive group, (2) block copolymerization using a monomer having an ion conductive group This is a method for producing a coalescence.

First, the first manufacturing method will be described.
Depending on the type, molecular weight, etc. of the monomer constituting the polymer block (A) or (B), the production method of the polymer block (A) or (B) can be a radical polymerization method, an anionic polymerization method, a cationic polymerization method, The method is appropriately selected from the coordination polymerization method and the like, but from the viewpoint of industrial ease, the radical polymerization method or the anion polymerization method is preferably selected. In particular, the so-called living polymerization method is preferable from the viewpoint of easy control of the molecular weight, molecular weight distribution and polymer structure, ease of bonding with the polymer block (B) or (A), and the like. A combined method or a living anionic polymerization method is preferred.

  In producing the block copolymer of the present invention by anionic polymerization, the styrenic derivative (I) alone is dissolved in an organic solvent, or other units described above that are different from the styrenic derivative (I). The polymer is dissolved in an organic solvent, an anionic polymerization initiator is added thereto, and an atmosphere of an inert gas such as nitrogen or argon is used at 0 to 100 ° C., particularly 20 to 70, under normal pressure or pressurized conditions. After polymerizing at a temperature of ° C. to produce a polymer (living polymer) constituting the polymer block (A), a monomer for producing the polymer block (B) was added to continue the polymerization. By adopting such a method, a block copolymer having a polymer block (A) and a polymer block (B) can be produced. In addition, after the polymer (living polymer) constituting the polymer block (B) is first produced, a monomer for producing the polymer block (A) is added thereto to perform polymerization, and polymerization is performed. A block copolymer having a combined block (A) and a polymer block (B) may be produced. When producing a multi-block copolymer consisting of a polymer block (A) and a polymer block (B) or having a polymer block (C) added to a triblock or more, the above-described polymerization operation is performed in the same manner as in the prior art. The desired multi-block copolymer can be produced by repeating the steps.

As the living anion polymerization initiator at that time, conventionally known living anion polymerization initiators such as alkyl lithium such as butyl lithium, ethyl lithium, and methyl lithium can be used. You may use individually or may use 2 or more types together. Among these, butyl lithium, particularly sec-butyl lithium, is preferably used from the viewpoint of the yield of the block copolymer, the polymerization initiation rate, and the like. The amount of the living anionic polymerization initiator used is generally from 0.000001 to 0.1% by mass, particularly from 0.000001 to 0.01% by mass, based on the total mass of the monomers obtained. This is preferable from the viewpoint of the molecular weight of the polymer.
Moreover, as an organic solvent used at the time of living anion polymerization, hydrocarbon solvents, such as cyclohexane, toluene, and benzene, etc. are preferable, and these organic solvents can be used individually or in combination of 2 or more types.

  When the polymerization is completed, the polymerization is stopped by adding a polymerization terminator such as methanol or ethanol to the polymerization mixture (reaction solution) or by introducing the polymerization mixture into the above-mentioned polymerization terminator such as methanol. can do.

The styrene derivative (I) used for the production of the block copolymer of the present invention can be produced by a known method or a method analogous thereto.
The 1- (4-vinylphenyl) adamantane represented by the chemical formula (Ia) can be produced, for example, by the method described in Non-Patent Document 1.
Specifically, as shown in the following reaction formula (I), 1-bromoadamantane and benzene are subjected to a coupling reaction in the presence of potassium carbonate using a palladium / carbon catalyst (Pd / C) to give 1-phenyl. Adamantane is formed, and the 1-phenyladamantane is reacted with 1,1-dichloromethyl ether in dichloromethane in the presence of TiCl ₄ to formylate, and the resulting formylate is then triphenylated in tetrahydrofuran (THF). It can be produced by reacting phosphine methylene (also known as methylenetriphenylphosphorane) (Ph ₃ P═CH ₂ ) (Wittig olefin reaction).

  In addition, as shown in the following reaction formula (II), 1-phenyladamantane and phenylmagnesium bromide are reacted in dehydrated methylene chloride to produce 1-phenyladamantane, and the produced 1-phenyladamantane is produced. Was reacted with bromine in carbon tetrachloride to form 1- (4-bromophenyl) adamantane, and magnesium was added to THF under nitrogen atmosphere and refluxed to give 4-adamantyl-phenylmagnesium bromide in the reaction system. (Intermediate) is formed, and dimethylformamide (DMF) is added thereto and reacted in a nitrogen atmosphere to produce 1- (4-formylphenyl) adamantane [also known as: 4- (1-adamantyl) benzaldehyde]. The resulting 1- (4-formylphenyl) adamantane was added to methyltriphenyl Added Honiumuburomido and potassium tert- butoxide also by reacting in dehydrated THF 1- (4-vinylphenyl) adamantane [another name: 4- (1-adamantyl) styrene] can be produced.

  In addition, 3- (4-vinylphenyl) -1,1′-biadamantane represented by the chemical formula (Ib) is, for example, as shown in the following reaction formula (III), 1-bromoadamantane is n- Reaction with sodium in octane produces biadamantane, which reacts with bromine in carbon tetrachloride to produce 3-bromo-1,1'-biadamantane, to which phenylmagnesium bromide is dehydrated methylene chloride. In order to produce 3-phenyl 1,1′-biadamantane, which is reacted with bromine in carbon tetrachloride to produce 3- (4-bromophenyl) -1,1′-biadamantane, In addition, magnesium was added to THF in a nitrogen atmosphere and refluxed to form 4-biadamantyl-phenylmagnesium bromide (intermediate product) in the reaction system. Dimethylformamide (DMF) was added thereto and reacted in a nitrogen atmosphere to produce 3- (4-formylphenyl) -1,1′-biadamantane, and methyltriphenylphosphonium bromide and potassium tert-butoxide were added thereto. In addition, it can be produced by a reaction in dehydrated THF to produce 3- (4-vinylphenyl) -1,1′-biadamantane.

Other than 1- (4-vinylphenyl) adamantane and 3- (4-vinylphenyl) -1,1′-biadamantane, the styrenic derivatives (I) shown in the above general formulas (Ic) to (Ig ₂ ) And styrene derivative (I) other than those can also be manufactured by the method according to above-described reaction formula (I)-(III).

Next, a method for bonding an ion conductive group to the obtained block copolymer will be described.
First, a method for introducing a sulfonic acid group into the obtained block copolymer will be described. Sulfonation can be performed by a known sulfonation method. As such a method, an organic solvent solution or suspension of a block copolymer is prepared, a sulfonating agent is added and mixed, a method of adding a gaseous sulfonating agent directly to the block copolymer, etc. Is exemplified.

  Sulfonating agents used include sulfuric acid, a mixture of sulfuric acid and aliphatic acid anhydride, chlorosulfonic acid, a mixture of chlorosulfonic acid and trimethylsilyl chloride, sulfur trioxide, a mixture of sulfur trioxide and triethyl phosphate. Examples thereof include aromatic organic sulfonic acids represented by 2,4,6-trimethylbenzenesulfonic acid. Examples of the organic solvent to be used include halogenated hydrocarbons such as methylene chloride, linear aliphatic hydrocarbons such as hexane, cyclic aliphatic hydrocarbons such as cyclohexane, and the like. You may use it, selecting suitably from several combinations.

  A method for introducing a phosphonic acid group into the obtained block copolymer will be described. Phosphonation can be performed by a known phosphonation method. Specifically, for example, an organic solvent solution or suspension of a block copolymer is prepared, and the copolymer is reacted with chloromethyl ether or the like in the presence of anhydrous aluminum chloride to introduce a halomethyl group into the aromatic ring. Thereafter, there may be mentioned a method in which phosphorus trichloride and anhydrous aluminum chloride are added and reacted, followed by a hydrolysis reaction to introduce a phosphonic acid group. Alternatively, a method may be exemplified in which phosphorus trichloride and anhydrous aluminum chloride are added to the copolymer and reacted to introduce a phosphinic acid group into the aromatic ring, and then the phosphinic acid group is oxidized with nitric acid to form a phosphonic acid group.

As described above, the degree of sulfonation or phosphonation is preferably sulfonated or phosphonated until the ion exchange capacity of the block copolymer is 0.30 meq / g or more, and is 0.50 meq / g or more. Is more preferable. Thereby, practical ion conduction performance is obtained. The ion exchange capacity of the sulfonated or phosphonated block copolymer, or the sulfonation rate or phosphonation rate in the α-methylstyrene block in the block copolymer is determined by acid titration, infrared spectroscopy, nuclear It can be calculated using an analytical means such as magnetic resonance spectrum ( ¹ H-NMR spectrum) measurement.

The second production method of the block copolymer used in the present invention is a method for producing a block copolymer using at least one monomer having an ion conductive group.
Examples of the monomer having an ion conductive group include a monomer having an ion conductive group bonded to the aromatic vinyl compound mentioned in the description of the styrene derivative (I) or the copolymer block (A) different from the styrene derivative (I). A monomer is preferable, and a monomer in which an ion conductive group is bonded to the above-described aromatic vinyl compound is more preferable because of easy introduction of an ion conductive group. Specific examples of the monomer having an ion conductive group bonded to the aromatic vinyl compound described above include styrene sulfonic acid, α-alkyl-styrene sulfonic acid, vinyl naphthalene sulfonic acid, α-alkyl-vinyl naphthalene sulfonic acid, Vinyl anthracene sulfonic acid, α-alkyl-vinylanthracene sulfonic acid, vinyl pyrene sulfonic acid, α-alkyl-vinyl pyrene sulfonic acid, styrene phosphonic acid, α-alkyl-styrene phosphonic acid, vinyl naphthalene phosphonic acid, α-alkyl-vinyl Examples include naphthalene phosphonic acid, vinyl anthracene phosphonic acid, α-alkyl-vinyl anthracene phosphonic acid, vinyl pyrene phosphonic acid, α-alkyl-vinyl pyrene phosphonic acid. Among these, o-, m- or p-styrene sulfonic acid, α-alkyl-o-, m- or p-styrene sulfonic acid is particularly preferable from the viewpoint of industrial versatility and ease of polymerization.

  As the monomer containing an ion conductive group, a monomer in which an ion conductive group is bonded to a conjugated diene compound can also be used. Specifically, 1,3-butadiene-1-sulfonic acid, 1,3-butadiene-2-sulfonic acid, isoprene-1-sulfonic acid, isoprene-2-sulfonic acid, 1,3-butadiene-1-phosphonic acid, Examples include 1,3-butadiene-2-phosphonic acid, isoprene-1-phosphonic acid, isoprene-2-phosphonic acid, and the like.

  Examples of the monomer containing an ion conductive group include vinyl sulfonic acid, α-alkyl-vinyl sulfonic acid, vinyl alkyl sulfonic acid, α-alkyl-vinyl alkyl sulfonic acid, vinyl phosphonic acid, α-alkyl-vinyl phosphone. Acid, vinyl alkyl phosphonic acid, α-alkyl-vinyl alkyl phosphonic acid and the like can also be used. Among these, vinyl sulfonic acid and vinyl phosphonic acid are preferable. As the monomer containing ion conductivity, a (meth) acrylic monomer to which an ion conductive group is bonded can also be used. Specific examples include methacrylic acid, acrylic acid, 2-acrylamido-2-methyl-1-propanesulfonic acid, and the like.

  The ion conductive group may be introduced in the form of a salt neutralized with a suitable metal ion (for example, alkali metal ion) or counter ion (for example, ammonium ion). For example, a desired ion-conducting group is introduced by producing a polymer using sodium o-, m- or p-styrene sulfonate, or sodium α-methyl-o-, m- or p-styrene sulfonate. it can. Or the block copolymer which made the sulfonic acid group into the salt form can be obtained by ion-exchange by a suitable method.

The present invention also relates to a membrane-electrode assembly that is prepared by using the polymer electrolyte of the present invention, that is, a polymer electrolyte membrane that can be used for a polymer electrolyte fuel cell.
The polymer electrolyte membrane of the present invention may contain a softening agent as long as the effects of the present invention are not impaired. Softeners include petroleum-based softeners such as paraffinic, naphthenic or aroma-based process oils, paraffin, vegetable oil-based softeners, plasticizers, etc., and these may be used alone or in combination of two or more. it can.

  The polymer electrolyte membrane of the present invention further includes various additives as required, for example, phenol stabilizers, sulfur stabilizers, phosphorus stabilizers, light stabilizers, antistatic agents, mold release agents, flame retardants. , Foaming agents, pigments, dyes, brighteners, carbon fibers and the like may be contained singly or in combination of two or more. Specific examples of the stabilizer include 2,6-di-t-butyl-p-cresol, pentaerystyryl-tetrakis [3- (3,5-di-t-butyl-4-hydroxyphenyl) propionate], 1 , 3,5-trimethyl-2,4,6-tris (3,5-di-tert-butyl-4-hydroxybenzyl) benzene, octadecyl-3- (3,5-di-tert-butyl-4-hydroxy) Phenyl) propionate, triethylene glycol-bis [3- (3-tert-butyl-5-methyl-4-hydroxyphenyl) propionate], 2,4-bis- (n-octylthio) -6- (4-hydroxy- 3,5-di-t-butylanilino) -1,3,5-triazine, 2,2, -thio-diethylenebis [3- (3,5-di-t-butyl-4-hydroxyphenyl) propi Onate], N, N′-hexamethylenebis (3,5-di-tert-butyl-4-hydroxy-hydrodinamamide), 3,5-di-tert-butyl-4-hydroxy-benzylphosphonate-diethyl ester, tris -(3,5-di-tert-butyl-4-hydroxybenzyl) -isocyanurate, 3,9-bis {2- [3- (3-tert-butyl-4-hydroxy-5-methylphenyl) propionyloxy ] -1,1-dimethylethyl} -2,4,8,10-tetraoxaspiro [5,5] undecane and other phenolic stabilizers; pentaerythrityltetrakis (3-laurylthiopropionate), distearyl Sulfur such as 3,3′-thiodipropionate, dilauryl 3,3′-thiodipropionate, dimyristyl 3,3′-thiodipropionate Stabilizers: trisnonylphenyl phosphite, tris (2,4-di-t-butylphenyl) phosphite, diasteryl pentaerythritol diphosphite, bis (2,6-di-t-butyl-4-methylphenyl) ) Phosphorus stabilizers such as pentaerythritol diphosphite. These stabilizers may be used alone or in combination of two or more.

  The polymer electrolyte membrane of the present invention can be further added with an inorganic filler as required, as long as the effects of the present invention are not impaired. Specific examples of such inorganic fillers include talc, calcium carbonate, silica, glass fiber, mica, kaolin, titanium oxide and the like.

  From the viewpoint of ion conductivity, the content of the block copolymer of the present invention in the polymer electrolyte membrane of the present invention is preferably 60% by mass or more, more preferably 80% by mass or more, and 90% by mass. % Or more is even more preferable.

  As the method for preparing the polymer electrolyte membrane of the present invention, any method can be adopted as long as it is a normal method for such preparation. For example, the block copolymer constituting the polymer electrolyte of the present invention or the block copolymer can be used. By mixing the polymer and additives as described above with an appropriate solvent, dissolving or suspending the block copolymer, casting it into a plate such as glass, and removing the solvent under appropriate conditions, A method of obtaining a cast film having a desired thickness, a method of forming a film using a known method such as hot press molding, roll molding, or extrusion molding can be used.

  The solvent to be used is not particularly limited as long as it can prepare a cast solution having a viscosity capable of being cast without destroying the structure of the block copolymer. Specifically, halogenated hydrocarbons such as methylene chloride, aromatic hydrocarbons such as toluene, xylene, and benzene, linear aliphatic hydrocarbons such as hexane and heptane, and alicyclic hydrocarbons such as cyclohexane. Examples thereof include ethers such as tetrahydrofuran, alcohols such as methanol, ethanol, propanol and isopropanol, and mixed solvents thereof. Depending on the configuration of the block copolymer, the molecular weight, the ion exchange capacity, etc., one or a combination of two or more can be appropriately selected from the solvents exemplified above and used.

  The solvent removal conditions can be arbitrarily selected as long as the solvent can be completely removed at a temperature lower than the temperature at which the ion conductive group such as the sulfone group of the block copolymer of the present invention is removed. . In order to express desired physical properties, a plurality of temperatures may be arbitrarily combined, or a combination of ventilation and vacuum may be arbitrarily combined. Specifically, after preliminary drying for several hours under vacuum conditions at room temperature to about 60 ° C., drying for about 12 hours under vacuum conditions at 100 ° C. or higher, preferably at 100 to 120 ° C. Although the method etc. which remove a solvent on conditions can be illustrated, it is not limited to these.

  The thickness of the polymer electrolyte membrane of the present invention is appropriately selected according to the application. For example, when the membrane is used as an electrolyte membrane for a fuel cell, the thickness is preferably about 5 to 500 μm from the viewpoint of required performance, membrane strength, handling properties, and the like. When the film thickness is less than 5 μm, the mechanical strength of the film and the gas barrier property tend to be insufficient. On the contrary, when the film thickness is thicker than 500 μm, the electric resistance of the film increases and sufficient proton conductivity does not appear, so that the power generation characteristics of the battery tend to be lowered. The film thickness is more preferably 10 to 300 μm.

  Next, a membrane-electrode assembly using the polymer electrolyte membrane of the present invention will be described. The production of the membrane-electrode assembly is not particularly limited, and a known method can be applied. For example, a catalyst paste containing an ion conductive binder is applied on the gas diffusion layer by a printing method or a spray method and dried. To form a joined body of the catalyst layer and the gas diffusion layer, and then to join the two pairs of joined bodies with the catalyst layer on the inside and by hot pressing or the like on both sides of the polymer electrolyte membrane, There is a method in which a catalyst paste is applied to both sides of a polymer electrolyte membrane by a printing method or a spray method, dried to form a catalyst layer, and a gas diffusion layer is pressure-bonded to each catalyst layer by hot pressing or the like. As another production method, a solution or suspension containing an ion conductive binder is applied to both surfaces of the polymer electrolyte membrane and / or the catalyst layer surfaces of two pairs of gas diffusion electrodes, and the electrolyte membrane and the catalyst layer surface are bonded together. There is a method of joining by thermocompression bonding. In this case, the solution or suspension may be applied to either the electrolyte membrane or the catalyst layer surface, or may be applied to both. As another manufacturing method, first, the catalyst paste is applied to a base film made of polytetrafluoroethylene (PTFE) and dried to form a catalyst layer, and then two pairs of base films on the base film are formed. The catalyst layer is transferred to both sides of the polymer electrolyte membrane by thermocompression bonding, the base film is peeled off to obtain a joined body of the electrolyte membrane and the catalyst layer, and the gas diffusion layer is crimped to each catalyst layer by hot pressing. There is a way. In these methods, these methods may be performed in a state where the ion conductive group is made into a salt with a metal such as Na, and a treatment for returning to a proton type by an acid treatment after bonding may be performed.

  Examples of the ion conductive binder constituting the membrane-electrode assembly include existing perfluorosulfones such as “Nafion” (registered trademark, manufactured by DuPont) and “Gore-select” (registered trademark, manufactured by Gore). An ion conductive binder made of an acid polymer, an ion conductive binder made of sulfonated polyethersulfone or sulfonated polyetherketone, an ion conductive binder made of polybenzimidazole impregnated with phosphoric acid or sulfuric acid can be used. . Moreover, you may produce an ion conductive binder from the block copolymer which comprises the polymer electrolyte membrane of this invention. In order to further enhance the adhesion between the electrolyte membrane and the gas diffusion electrode, it is preferable to use an ion conductive binder formed from the same material as the polymer electrolyte membrane.

  The constituent material of the catalyst layer of the membrane-electrode assembly is not particularly limited as the conductive material / catalyst support, and examples thereof include carbon materials. Examples of the carbon material include carbon black such as furnace black, channel black, and acetylene black, activated carbon, graphite, and the like. These may be used alone or in combination of two or more. The catalyst metal may be any metal that promotes the oxidation reaction of fuel such as hydrogen and methanol and the reduction reaction of oxygen, such as platinum, gold, silver, palladium, iridium, rhodium, ruthenium, iron, Cobalt, nickel, chromium, tungsten, manganese, palladium, etc., or alloys thereof, for example, platinum-ruthenium alloys are mentioned. Of these, platinum and platinum alloys are often used. The particle size of the metal serving as a catalyst is usually 10 to 300 angstroms. When these catalysts are supported on a conductive material such as carbon / catalyst support, the amount of catalyst used is small and it is advantageous in terms of cost. The catalyst layer may contain a water repellent as necessary. Examples of the water repellent include various thermoplastic resins such as polytetrafluoroethylene, polyvinylidene fluoride, styrene-butadiene copolymer, and polyetheretherketone.

  The gas diffusion layer of the membrane-electrode assembly is made of a material having conductivity and gas permeability, and examples of such a material include porous materials made of carbon fibers such as carbon paper and carbon cloth. Moreover, in order to improve water repellency, this material may be subjected to water repellency treatment.

A polymer electrolyte fuel obtained by inserting the membrane-electrode assembly obtained by the above-described method between a conductive separator material that also serves as a gas supply flow path to the electrode and the electrode chamber separation. A battery is obtained. The membrane-electrode assembly of the present invention uses a pure hydrogen type using hydrogen as a fuel gas, a methanol reforming type using hydrogen obtained by reforming methanol, and hydrogen obtained by reforming natural gas. Natural gas reforming type, gasoline reforming type using hydrogen obtained by reforming gasoline, direct methanol type using methanol directly, etc. can be used as a membrane-electrode assembly for polymer electrolyte fuel cells. is there.
The fuel cell using the polymer electrolyte membrane of the present invention is excellent in chemical stability, has little deterioration in power generation characteristics over time, and can be used stably for a long time.

Hereinafter, the present invention will be described more specifically with reference to Examples, Comparative Examples, and Reference Examples, but the present invention is not limited to these examples. In addition, the chemical | medical agent (compound etc.) used in the following examples used the highest purity as long as it was available. The solvent used was sufficiently degassed.
Confirmation of the structure of the product (intermediate compound, final compound) obtained in Reference Example 1 and Reference Example 2, progress of polymerization, measurement of the number average molecular weight and molecular weight distribution of the polymer obtained in each Example, Mechanical viscoelasticity test and proton conductivity measurement were performed as follows.

(1) Confirmation of product structure:
The product (intermediate compound, final compound) produced in the following Reference Example 1 or Reference Example 2 was dissolved in deuterated chloroform, and a proton nucleus ( ¹ ) was prepared using a nuclear magnetic resonance apparatus (“BRUCKER DPX300” manufactured by Bruker). The magnetic resonance spectra of H) and carbon nuclei ( ¹³ C) were measured at 27 ° C. to confirm their structures. In addition, for some of the products generated in Reference Example 2, the infrared absorption spectrum was measured by the KBr method using an infrared analyzer “FT / IR-460” manufactured by JASCO Corporation in confirming the structure.

(2) Measurement of polymerization progress:
About the solution obtained by dissolving the polymerization reaction solution or polymer produced in the following examples in deuterated chloroform, using a nuclear magnetic resonance spectrometer (“JNMLA400” manufactured by JEOL Datum), the proton nucleus ( ¹ H) A magnetic resonance spectrum was measured at 50 ° C. to measure the degree of polymerization.

(3) Measurement of number average molecular weight (Mn) and molecular weight distribution (Mw / Mn):
Using standard polystyrene having a known peak molecular weight and using a gel permeation chromatograph (GPC) calibrated with the standard polystyrene (“HLC-8020” manufactured by Tosoh Corporation), the number average molecular weight (Mn) and weight average of the polymer Molecular weight (Mw) was measured (developing solvent: tetrahydrofuran, temperature: 40 ° C.). Molecular weight distribution was calculated | required as ratio (Mw / Mn) of a weight average molecular weight (Mw) and a number average molecular weight (Mn).

(4) Measurement of ion exchange capacity A sample was weighed (a (g)) in a glass container that could be sealed, and an excess amount of a saturated aqueous sodium chloride solution was added thereto and stirred overnight. Hydrogen chloride generated in the system was titrated (b (ml)) with a 0.01N NaOH standard aqueous solution (titer f) using a phenolphthalein solution as an indicator. The ion exchange capacity was determined by the following formula.
Ion exchange capacity = (0.01 × b × f) / a

(5) Measurement of proton conductivity A sample of 1 cm × 4 cm was sandwiched between a pair of platinum black-plated platinum electrodes and attached to an open cell. The measurement cell was installed in a constant temperature and humidity chamber adjusted to a temperature of 80 ° C. and a relative humidity of 90%, and proton conductivity was measured by an AC impedance method.

(6) Dynamic viscoelasticity test:
Using the membranes obtained in Examples or Comparative Examples, using a wide-range dynamic viscoelasticity measuring device (“DVE-V4FT Rheospectr” manufactured by Rheology), in the tension mode (frequency 11 Hz), The storage elastic modulus E ′, the loss elastic modulus E ″ and the loss tangent tan were measured at 3 ° C. per minute, and the peak temperature of the loss tangent was defined as Tα (° C.). Tα is a characteristic value according to the glass transition temperature indicating the heat resistance of the polymer.

<< Reference Example 1 >> [Production of 1- (4-vinylphenyl) adamantane]
1- (4-Vinylphenyl) adamantane was produced as follows according to the above reaction formula (II).
(1) Production of 1-phenyladamantane:
Under a nitrogen atmosphere, 20 ml of dehydrated ether was added to 3.36 g (138.0 mmol) of magnesium, and then a few drops of 1,2-dibromoethane were added to activate the surface of magnesium. Next, 100 ml of a dehydrated ether solution of 10 ml (84 mmol) of bromobenzene was added dropwise and stirred at room temperature for 3 hours, and then the ether was distilled off under reduced pressure to obtain a gray solid of phenylmagnesium bromide. To this gray solid was added 5.00 g (23.2 mmol) of 1-bromoadamantane and 70 ml of dehydrated methylene chloride, and refluxed until the consumption of 1-bromoadamantane was completely confirmed while monitoring the reaction by GC and NMR. (After about 24 hours) The system was cooled to 0 ° C., water was added to stop the reaction, and 2N hydrochloric acid was further added. Extraction was performed 3 times with methylene chloride, and the organic layer was washed 3 times with water. The organic layer was dried by adding anhydrous magnesium sulfate, the magnesium sulfate was filtered off, and the organic solvent was distilled off under reduced pressure to obtain 4.52 g of a pale yellow solid. The pale yellow solid was purified by silica gel column chromatography using hexane as a developing solvent to obtain 8.45 g of a white solid, and then the white solid was recrystallized from methanol. -A white solid (mp84-85 ° C) of 6.30 g (yield 64%) of phenyladamantane was obtained.

¹ H-NMR (CDCl ₃ ): δ 1.73-1.82 (m, 6H, C (2) H ₂ ), 1.92 (s, 6H, C (4) H ₂ ), 2.10 (S, 3H, C (3) H), 7.15-7.20 (m, 1H, C (d) H), 7.29-7.39 (m, 4H, C (b) H, C (C) H)
_{^{· 13 C-NMR (CDCl 3}} ): δ 29.0 (C-3), 36.2 (C-1), 36.9 (C-2), 43.2 (C-4), 124.9 (Cc), 125.6 (Cd), 128.2 (Cb), 151.4 (Ca)

(2) Production of 1- (4-bromophenyl) adamantane:
After 34 ml of carbon tetrachloride was added to 3.60 g (17.0 mmol) of 1-phenyladamantane obtained in (1) above, 17 ml (330 mmol) of bromine was added and stirred at room temperature for 4 hours. The reaction solution was poured into ice water, excess bromine was treated with sodium bisulfite, extracted three times with methylene chloride, the organic layer was washed three times with water, and anhydrous magnesium sulfate was added to the organic layer and dried. . After filtering off magnesium sulfate, the organic solvent was distilled off under reduced pressure to obtain 4.95 g of 1- (4-bromophenyl) adamantane having the following physical properties (yield 100%, white solid, mp 101-102 ° C.). It was.
¹ H-NMR (CDCl ₃ ): δ 1.71-1.81 (m, 6H, C (2) H ₂ ), 1.87 (s, 6H, C (4) H ₂ ), 2.09 (S, 3H, C (3) H), 7.21-7.24 (d, 2H, C (c) H, J = 8.6 Hz), 7.40-7.43 (d, 2H, C (B) H, J = 8.6 Hz)
_{^{· 13 C-NMR (CDCl 3}} ): δ 28.9 (C-3), 36.1 (C-1), 36.7 (C-2), 43.1 (C-4), 119.3 (Cd), 126.9 (Cc), 131.1 (Cb), 150.4 (Ca)

(3) Production of 1- (4-formylphenyl) adamantane:
Under a nitrogen atmosphere, 20 ml of dehydrated THF was added to 0.84 g (35 mmol) of magnesium, and then a few drops of 1,2-dibromoethane were added to activate the surface of magnesium. To this, 40 ml of a dehydrated THF solution of 4.95 g (17.0 mmol) of 1- (4-bromophenyl) adamantane obtained in (2) above was added dropwise at room temperature and then refluxed. During the reflux, the reaction was monitored by gas chromatography, and when 1- (4-bromophenyl) adamantane was completely consumed and production of 1-phenyladamantane derived from 4-adamantyl-phenylmagnesium bromide was confirmed ( After about 2 hours), the system was cooled to 0 ° C., and 25 ml (323 mmol) of dehydrated DMF was added dropwise. Then, after stirring overnight at room temperature, water was added to the system to stop the reaction, and 2N hydrochloric acid was further added to treat excess magnesium. After THF was removed by evaporation, extraction was performed 3 times with methylene chloride and the organic layer was washed 3 times with water, and anhydrous magnesium sulfate was added to the organic layer and dried. After filtering off magnesium sulfate, the organic solvent was distilled off under reduced pressure to obtain 4.87 g of a pale yellow solid. This was subjected to chromatography using hexane as a developing solvent to remove 1.01 g (4.76 mmol, recovery rate 28%) of 1-phenyladamantane as a by-product, and then hexane / ethyl acetate = 20. / 1, 10/1 (v / v) was used as a developing solvent to obtain 3.25 g of a white solid. This was purified by sublimation (120 to 130 ° C./0.2 mmHg), and 2.88 g of 1- (4-formylphenyl) adamantane [also known as: 4- (1-adamantyl) benzaldehyde] having the following physical properties (yield 70). %, White powder, mp 253-255 ° C.).

¹ H-NMR (CDCl ₃ ): δ 1.74-1.84 (m, 6H, C (2) H ₂ ), 1.94 (s, 6H, C (4) H ₂ ), 2.13 (S, 3H, C (3) H), 7.51-7.54 (d, 2H, C (c) H, J = 8.3 Hz), 9.98 (s, 1H, CHO)
_{^{· 13 C-NMR (CDCl 3}} ): δ 28.8 (C-3), 36.7 (C-2), 37.0 (C-1), 42.9 (C-4), 125.7 (Cc), 129.8 (Cb), 134.2 (Cd), 158.6 (Ca), 192.2 (CHO)
IR (KBr): 2903 and 2848 cm ⁻¹ (C—H stretching vibration), 1698, 1686 and 1654 cm ⁻¹ (C═O stretching vibration), 1604 cm ⁻¹ (aromatic ring C—C vibration), 1448, 1167, 802 cm ⁻¹ (C-H bending vibration)

(4) Production of 1- (4-vinylphenyl) adamantane:
Under a nitrogen atmosphere, 1.97 g (17.6 mmol) of potassium tert-butoxide was added to 4.59 g (12.5 mmol) of methyltriphenylphosphonium bromide, and then 95 ml of dehydrated THF was added and stirred at room temperature for about 20 minutes. . After cooling the system to 0 ° C., 45 ml of a dehydrated THF solution of 2.61 g (10.9 mmol) of 1- (4-formylphenyl) adamantane obtained in (3) above was added dropwise and stirred overnight at room temperature. . After the consumption of 1- (4-formylphenyl) adamantane was completely confirmed by gas chromatography, water was added to the system to stop the reaction. After THF was removed by evaporation, extraction was performed three times with ether and the organic layer was washed twice with water, and anhydrous magnesium sulfate was added to the organic layer and dried. After filtering off magnesium sulfate, the organic solvent was distilled off under reduced pressure to obtain a white solid. This is dissolved in a small amount of THF and poured into a large amount of hexane to precipitate the triphenylphosphine oxide produced by the reaction. After removing the triphenylphosphine oxide by filtration, the organic solvent is distilled off under reduced pressure. .94 g of a white solid was obtained. This white solid was purified by silica gel chromatography using hexane as a developing solvent to obtain 3.45 g of white powder. This white powder was recrystallized from methanol to give 2.08 g (8.72 mmol, yield 80%, white needle crystal, mp 98-99 ° C.) of 1- (4-vinylphenyl) adamantane having the following physical properties. Obtained.

¹ H-NMR (CDCl ₃ ): δ 1.72-1.82 (m, 6H, C (2) H ₂ ), 1.91 (s, 6H, C (4) H ₂ ), 2.10 _{(s, 3H, C (3} ) H), 5.17-5.21 (d, 1H, CH 2 = trans, J = 11.1Hz), 5.68-5.74 (d, 1H, CH 2 = Cis, J = 17.7 Hz), 6.65-6.75 (d, 1H, = CH, J = 11.1 Hz and 17.7 Hz), 7.31-7.39 (m, 4H, C ( b) H and C (c) H).
* ¹³ C-NMR (CDCl ₃ ): δ 29.0 (C-3), 36.2 (C-1), 36.9 (C-2), 43.2 (C-4), 113.1 (CH ₂ =), 125.1 (Cc), 126.1 (Cb), 135.0 (Cd), 136.7 (= CH), 151.2 (Ca)
IR (KBr): 2917, 2903 and 2847 cm ⁻¹ (C—H stretching vibration), 1629 cm ⁻¹ (C = C stretching vibration), 1510, 1446, 1345, 888, 897, 838 and 808 cm ⁻¹ (C— H bending vibration)

<< Example 1 >> From [hydrogenated {1- (4-vinylphenyl) adamantane / styrene copolymer block}-{polyisoprene block}-{1- (4-vinylphenyl) adamantane / styrene copolymer block} Of a sulfonated product of a triblock copolymer]
(a) A triblock copolymer comprising {1- (4-vinylphenyl) adamantane / styrene copolymer block}-{polyisoprene block}-{1- (4-vinylphenyl) adamantane / styrene copolymer block} Synthesis of Polymer] (1) After replacing the gas in the dried glass container with nitrogen gas, 2.087 g (8.76 mmol) of 1- (4-vinylphenyl) adamantane and 0.912 g of styrene (8. Next, 25 ml of cyclohexane was added as a solvent to dissolve 1- (4-vinylphenyl) adamantane and styrene to prepare a monomer mixture solution. The density of this monomer mixture solution was 0.7804 g / ml. From this point, the concentrations of 1- (4-vinylphenyl) adamantane and styrene in the solution were both 0.304 mol / liter.
(2) After replacing the gas in the dry glass reaction vessel with nitrogen gas, 50 ml of cyclohexane was added and heated to 50 ° C., and then 0.081 ml of a cyclohexane solution of sec-butyllithium (0 sec as sec-butyllithium). .105 mmol) and 8.65 ml of the monomer mixture solution prepared in (1) above (containing 2.63 mmol of 1- (4-vinylphenyl) adamantane and 2.63 mmol of styrene). Then, after polymerization at 50 ° C. for 30 minutes, a part of the reaction solution was sampled and GPC measurement was performed. It was.

(3) Subsequently, 4.2 g (61.7 mmol) of isoprene was added to the reaction vessel of (2), and polymerization was performed at 50 ° C. for 1.5 hours. When a part of the reaction solution was sampled and GPC measurement was performed, a polymer having a number average molecular weight (Mn) of 107,000 and an average molecular weight of 1.02 was produced. Subsequently, 8.65 ml [containing 2.63 mmol of 1- (4-vinylphenyl) adamantane and 2.63 mmol of styrene] of the mixed monomer solution prepared in the above (1) was added to the reaction vessel at 50 ° C. The polymerization reaction was carried out for 1 hour, and a small amount of degassed methanol was added to terminate the polymerization.
(4) A part of the reaction solution obtained in (3) above was sampled and subjected to GPC measurement. As a result, a block copolymer having a number average molecular weight (Mn) of 114000 and a molecular weight distribution (Mw / Mn) of 1.03 was obtained. Was generated. The obtained block copolymer solution (reaction solution) was washed with water, and then precipitated and recovered with a methanol / acetone mixed solvent. When ¹ H-NMR measurement of the resulting block copolymer was performed, the obtained block copolymer was {1- (4-vinylphenyl) adamantane / styrene copolymer block}-{polyisoprene. Block}-{1- (4-vinylphenyl) adamantane / styrene copolymer block}, and the polyisoprene block contains 5.5% of 3,4-linkage, The content ratio of 1- (4-vinylphenyl) adamantane / styrene copolymer block based on the mass of the block copolymer was 28.7% by mass.

(B) [hydrogenated {1- (4-vinylphenyl) adamantane / styrene copolymer block}-{polyisoprene block}-{1- (4-vinylphenyl) adamantane / styrene copolymer block} Synthesis of Block Copolymer] (1) A triblock copolymer [{1- (4-vinylphenyl) adamantane / styrene copolymer block} produced in Example 1 (a) was placed in a dry glass reaction vessel. -{Polyisoprene block}-{1- (4-vinylphenyl) adamantane / styrene copolymer block} triblock copolymer] 3.6 g, antioxidant ("Irganox, manufactured by Ciba-Geigy, Japan)
1010 ") and 0.36 g of p-toluenesulfonic acid hydrazide were added and vacuum deaeration was performed for 30 minutes. Thereafter, nitrogen gas was introduced into the reaction vessel, 250 ml of xyle was added, stirred and heated to 120 ° C. The solution was initially in a suspended state, but when heated to 120 ° C., it became a homogeneous solution, and generation of bubbles due to generation of nitrogen gas and hydrogen gas was confirmed. The reaction was continued for 15 hours while maintaining the temperature of the reaction solution at 120 ° C. After completion of the reaction, the reaction solution was cooled to room temperature and then poured into a large excess of methanol to precipitate and recover the hydrogenated triblock copolymer. The recovered hydrogenated triblock copolymer is dissolved in toluene and then reprecipitated with methanol, and the purification is repeated three more times, and the resulting hydrogenated triblock copolymer is purified overnight at 50 ° C. Vacuum dried.
(2) As a result of ¹ H-NMR measurement of the hydrogenated triblock copolymer obtained in the above (1), most of the peaks derived from double bonds in isoprene disappeared, and the hydrogenation rate Was 98%. Moreover, when the GPC measurement of the hydrogenated triblock copolymer was performed, the peak which shows gelatinization and decomposition | disassembly was not observed but they were number average molecular weight (Mn) 122000 and molecular weight distribution (Mw / Mn) 1.03.

(C) A trihydrate comprising [hydrogenated {1- (4-vinylphenyl) adamantane / styrene copolymer block}-{polyisoprene block}-{1- (4-vinylphenyl) adamantane / styrene copolymer block}. Synthesis of Sulfonated Compound of Block Copolymer] (1) [Hydrogenated {1- (4-vinylphenyl) adamantane / styrene copolymer block}-{polyisoprene block} obtained in Example 1 (b) -Triblock copolymer consisting of {1- (4-vinylphenyl) adamantane / styrene copolymer block} After vacuum drying in a glass reaction vessel equipped with a stirrer for 1 hour and then substituting with nitrogen Then, 1000 ml of methylene chloride was added and dissolved by stirring at 35 ° C. for 2 hours. After dissolution, a sulfating reagent obtained by reacting 25.0 ml of acetic anhydride and 11.2 ml of sulfuric acid at 0 ° C. in 49.9 ml of methylene chloride was gradually added dropwise over 20 minutes. After stirring at 35 ° C. for 20 hours, the polymer solution was poured into 2 L of distilled water while stirring to coagulate and precipitate the polymer. The precipitated solid was washed with distilled water at 90 ° C. for 30 minutes and then filtered. This washing and filtration operation was repeated until there was no change in the pH of the washing water, and the finally collected polymer was vacuum-dried to obtain a finally obtained sulfonated block copolymer. The sulfonation rate of the benzene ring in the obtained sulfonated block copolymer was 32.5 mol% from ¹ H-NMR analysis, and the ion exchange capacity was 0.52 meq / g.

(D) Preparation of polymer electrolyte membrane A 5% by mass THF / MeOH (mass ratio 8/2) solution of the sulfonated block copolymer obtained in Example 1 (c) was prepared, and a polytetrafluoroethylene sheet was prepared. The film was cast at a thickness of about 1000 μm and sufficiently dried at room temperature to obtain a film having a thickness of 50 μm.

Comparative Example 1 Synthesis of Sulfonated SEBS (a) Synthesis of Sulfonated SEBS A sulfated reagent was prepared by reacting 17.1 ml of acetic anhydride and 7.64 ml of sulfuric acid at 0 ° C. in 34.2 ml of methylene chloride. . On the other hand, 100 g of SEBS (styrene- (ethylene-butylene) -styrene) block copolymer [“Septon 8007” manufactured by Kuraray Co., Ltd.] was vacuum-dried in a glass reaction vessel equipped with a stirrer for 1 hour, and then nitrogen. After the replacement, 1000 ml of methylene chloride was added and dissolved by stirring at 35 ° C. for 4 hours. After dissolution, the sulfating reagent was gradually added dropwise over 20 minutes. After stirring at 35 ° C. for 5 hours, the polymer solution was poured into 2 L of distilled water while stirring to coagulate and precipitate the polymer. The precipitated solid was washed with distilled water at 90 ° C. for 30 minutes and then filtered. This washing and filtration operation was repeated until there was no change in the pH of the washing water, and finally the polymer collected by filtration was vacuum dried to obtain sulfonated SEBS. The sulfonation rate of the benzene ring of the styrene unit of the obtained sulfonated SEBS was 19.3 mol% from ¹ H-NMR analysis, and the ion exchange capacity was 0.51 meq / g.

(B) Production of polymer electrolyte membrane A membrane having a thickness of 50 µm was obtained in the same manner as in Example 1 (d) except that the sulfonated SEBS obtained in Comparative Example 1 (a) was used.

<< Comparative Example 2 >>
A DuPont Nafion film (Nafion 112) was selected as the perfluorocarbon sulfonic acid polymer electrolyte. The film had a thickness of about 50 μm and an ion exchange capacity of 0.91 meq / g.

  Tα before sulfonation of the polymer electrolyte obtained in Example 1 and the polymer electrolytes of Comparative Examples 1 and 2, sulfonation rate of the polymer electrolyte membrane formed after sulfonation, ion exchange capacity, proton conductivity, Table 1 shows the values of Tα obtained from the dynamic viscoelasticity measurement.

As is apparent from Table 1, the block copolymer obtained by the present invention has very high heat resistance in addition to high ionic conductivity.
Since the polymer electrolyte of the present invention is extremely excellent in heat resistance, the polymer electrolyte is suitably used for polymer electrolyte applications requiring heat resistance by taking advantage of its properties. In particular, when preparing a polymer electrolyte membrane for a polymer electrolyte fuel cell, which requires stable operation under high temperature conditions, or a membrane-electrode assembly or membrane-electrode assembly using this membrane It is used suitably for the binder used for. Furthermore, it is also suitably used for soft actuators (robots, artificial muscles, therapeutic / nursing aids) and various gas sensors (for example, hydrogen sensors) that require heat resistance.

Claims (14)

The following general formula (I);

(In the formula, R ¹ represents an alicyclic hydrocarbon group having a polycyclic structure, and R ² represents a hydrogen atom, an alkyl group having 1 to 10 carbon atoms, or an aryl group.)
A block having a polymer block (A) having a structural unit derived from a styrene derivative represented by the formula (B) and a flexible polymer block (B) and having an ion conductive group in the polymer block (A) A polymer electrolyte made of a copolymer. The polymer electrolyte according to claim 1, wherein R ¹ in the general formula (I) is a bridged alicyclic hydrocarbon group.   As structural units derived from the styrene derivative represented by the general formula (I), structural units derived from 1- (4-vinylphenyl) adamantane and 3- (4-vinylphenyl) -1,1′-biadamantane The polymer electrolyte according to claim 1, which has at least one kind of structural unit derived from the above.   The polymer according to any one of claims 1 to 3, wherein a proportion of the structural unit derived from the styrene derivative represented by the general formula (I) in the polymer block (A) is 10% by mass or more. Electrolytes.   The polymer electrolyte according to any one of claims 1 to 4, wherein the mass ratio of the polymer block (A) to the polymer block (B) is 95: 5 to 5:95. In the structural unit derived from a styrene derivative represented by the general formula (I), the polymer described in any one of claims 1 to 5 R ² is an alkyl group or an aryl group having from 1 to 4 carbon atoms Electrolytes.   The polymer block (B) is an alkene unit having 2 to 8 carbon atoms, a cycloalkene unit having 5 to 8 carbon atoms, and at least a part of the carbon-carbon double bond may be hydrogenated. The vinylcycloalkene unit, at least a part of the carbon-carbon double bond may be hydrogenated, or the conjugated diene unit having 4 to 8 carbon atoms and at least a part of the carbon-carbon double bond may be hydrogenated The polymer electrolyte according to any one of claims 1 to 6, which is a polymer block composed of at least one repeating unit selected from the group consisting of a good conjugated cycloalkadiene unit having 5 to 8 carbon atoms.   The polymer block (B) is at least selected from the group consisting of alkene units having 2 to 8 carbon atoms and conjugated diene units having 4 to 8 carbon atoms in which at least part of the carbon-carbon double bond may be hydrogenated. The polymer electrolyte according to any one of claims 1 to 6, which is a polymer block composed of one type of repeating unit. In the general formula (I), R ² is a methyl group, and the polymer block (B) is composed of a conjugated diene unit having 4 to 8 carbon atoms in which at least a part of the carbon-carbon double bond may be hydrogenated. The electrolyte according to any one of claims 1 to 5. (Wherein, M represents a hydrogen atom, an ammonium ion or an alkali metal ion) ion-conducting group is -SO ₃ M or _-PO 3 HM to any one of claims 1 to 9 is a group represented by The polymer electrolyte described. 11. The polymer electrolyte according to claim 1, wherein the block copolymer has an ion exchange capacity of 0.30 meq / g or more.   The film | membrane containing the polymer electrolyte of any one of Claims 1-11. A membrane-electrode assembly using the electrolyte membrane according to claim 12. A polymer electrolyte fuel cell using the membrane-electrode assembly according to claim 13.