JP2009173898A - Hydrocarbon anion exchange membrane, and manufacturing method therefor - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide an anion exchange membrane having a high moisture content, low electric resistance and excellent ion conductivity, a manufacturing method therefor, and a fuel cell diaphragm capable of providing an anion type fuel cell of high output. <P>SOLUTION: This hydrocarbon anion exchange membrane is filled with an anion exchange resin in a pore part of a porous membrane, by reacting an anion exchange membrane precursor obtained by polymerizing a polymerizable composition containing an aromatic polymerizable monomer having a halogeno alkyl group, after impregnated into a porous membrane, with a polyamine. The ion exchange resin has an aromatic ring, and the aromatic ring is bonded with a group having a plurality of anion exchange groups, in the hydrocarbon anion exchange membrane. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

  The present invention relates to a hydrocarbon-based anion exchange membrane and a method for producing the same. The diaphragm has a group having a plurality of anion exchange groups in the hydrocarbon polymer material forming the anion exchange membrane, has a high water content, a low membrane resistance, and a useful ion conductivity. It is.

  A polymer electrolyte fuel cell is a fuel cell using a solid polymer such as an ion exchange resin as an electrolyte, and has a feature that its operating temperature is relatively low. As shown in FIG. 1, the solid polymer fuel cell includes a solid polymer electrolyte membrane 6 in a space in the battery partition wall 1 having a fuel gas flow hole 2 and an oxidant gas flow hole 3 communicating with the outside. The fuel chamber 7 and the oxidant gas flow hole 3 are connected to the outside through the fuel gas flow hole 2 and partitioned by a joined body in which the fuel chamber side gas diffusion electrode 4 and the oxidant chamber side gas diffusion electrode 5 are joined to both surfaces of It has a basic structure in which an oxidant chamber 8 communicating with the outside is formed. In the polymer electrolyte fuel cell having such a basic structure, a fuel made of hydrogen gas or methanol is supplied to the fuel chamber 7 through the fuel flow hole 2 and the oxidant gas flow hole 3 is passed to the oxidant chamber 8. Electric energy is generated by the following mechanism by supplying oxygen-containing gas such as oxygen or air as an oxidant and connecting an external load circuit between the gas diffusion electrodes.

  Until now, research and development of cation exchange membrane fuel cells using a cation exchange electrolyte membrane (hereinafter also referred to as cation exchange membrane) as the solid polymer electrolyte membrane 6 have been actively conducted. In recent years, an anion exchange membrane fuel cell using an anion exchange electrolyte membrane (hereinafter also referred to as an anion exchange membrane) as the solid polymer electrolyte membrane 6 has been proposed. In the anion exchange membrane fuel cell, hydroxide ions are conducted through the solid polymer electrolyte membrane 6 and move from the oxidant gas chamber 12 side to the fuel chamber 11 side. That is, when a liquid fuel such as hydrogen or a methanol aqueous solution is supplied to the fuel chamber 11 and oxygen and water are supplied to the oxidant gas chamber 12, the catalyst and oxygen contained in the electrode in the oxidant gas chamber side catalyst electrode layer 5 are supplied. Hydroxide ions are generated by contact with water, and the generated hydroxide ions are conducted through the solid polymer electrolyte membrane 6 and move to the fuel chamber 11 side. Reacts to produce water. Further, electrons are generated simultaneously with water in the fuel chamber side catalyst electrode layer 4, and the generated electrons move to the oxidant gas chamber side catalyst electrode layer 5 through an external load circuit.

Such an anion exchange membrane fuel cell has the following advantages not found in a cation exchange membrane fuel cell.
(I) Since the reaction field is strongly basic, an inexpensive transition metal catalyst can be used.
(Ii) Since there are a wide variety of catalyst types, it is possible to increase the output of the battery and use various fuels.
(Iii) Since the movement direction of the hydroxide ions in the electrolyte is opposite to the permeation direction of the fuel to the oxidant gas electrode, the fuel permeation to the oxidant gas electrode is suppressed, and the fuel and the oxidant gas directly It is possible to prevent an increase in overvoltage due to reaction and suppress a decrease in output voltage.

  It is also possible to reduce the cost by using an inexpensive hydrocarbon-based material as a raw material for the anion exchange membrane. For this reason, several fuel cells using an anion exchange type electrolyte membrane have been proposed as solid polymer type fuel cells replacing the cation exchange membrane type fuel cells.

  In an anion type fuel cell membrane comprising a hydrocarbon-based anion exchange membrane having such advantages, the anion exchange groups used in the hydrocarbon-based anion exchange membrane include excellent ion conductivity and Quaternary ammonium groups are often used because of the availability of raw materials for producing the anion exchange membrane. Here, a hydrocarbon-based anion exchange membrane having such a quaternary ammonium group as an anion exchange group (hereinafter, this anion exchange membrane is also simply referred to as a quaternary ammonium type anion exchange membrane) is usually chloromethyl. A polymerizable composition comprising an aromatic polymerizable monomer having a halogenoalkyl group, such as styrene, and a crosslinkable polymerizable monomer is brought into contact with the porous film, and the polymerizable composition is used for the porous film. In general, it is produced by filling the voids having polymerization and then polymerizing, and then converting the halogenoalkyl group into a quaternary ammonium group. As a result, it has been reported that an anion exchange membrane fuel cell having excellent durability and excellent permeation suppression of fuel such as methanol can be provided (Patent Documents 1 and 2).

  However, when an anionic fuel cell is assembled and operated using such a quaternary ammonium hydrocarbon anion exchange membrane as a solid polymer electrolyte membrane, the moisture content is low and the electrical resistance is expected. In addition, since hydroxide ions having a diameter larger than that of protons move in the membrane, it was found that the hydroxide ion conductivity was inferior to one step and it was difficult to obtain a high battery output.

  In order to reduce the electrical resistance of the anion exchange membrane, the film thickness must be reduced considerably, or the degree of crosslinking must be significantly reduced to increase the water content, and the number of ion exchange groups must be increased. In this case, it is difficult to keep the strength of the film sufficiently contrary to the improvement of the above physical properties, or the increase in the number of ion exchange groups due to the reduction in the degree of crosslinking is physically limited. It was difficult to get output.

JP-A-11-135137 Japanese Patent Laid-Open No. 11-273695

  Thus, in an anionic fuel cell using a quaternary ammonium hydrocarbon anion exchange membrane as a solid polymer electrolyte membrane, the water content of the membrane is high, the electric resistance is low, and the ion conductivity is excellent. Nothing has been known that can provide a high battery output. Against this background, the first object of the present invention is to provide an anion exchange membrane having a high water content, low electrical resistance, and excellent ion conductivity. A second object of the present invention is to provide a method for producing the anion exchange membrane, and a third object is to provide a membrane for a fuel cell that can provide a high-power anion fuel cell.

  The present inventors have conducted extensive research in view of the above problems. As a result, the present inventors have succeeded in developing a hydrocarbon-based anion exchange membrane that can satisfactorily solve the problem, and have proposed the present invention.

  That is, the present invention relates to a hydrocarbon-based anion exchange membrane in which an anion exchange resin is filled in a void portion of a porous membrane, the ion exchange resin having an aromatic ring, and the aromatic A hydrocarbon-based anion exchange membrane in which a group having a plurality of anion-exchange groups is bonded to a ring, a method for producing the same, and a diaphragm for an anionic fuel cell comprising the hydrocarbon-based anion exchange membrane.

  The hydrocarbon-based anion exchange membrane of the present invention has a large ion exchange capacity, resulting in a high water content and a low membrane resistance. Furthermore, it is possible to increase the hydroxide ion conduction site, and to express high ion conductivity. Therefore, when this is used for an anionic fuel cell as a diaphragm, the membrane resistance can be suppressed, the internal resistance of the battery is low, and the anion conductivity is excellent, so that a high battery output can be obtained.

  The hydrocarbon-based anion exchange membrane of the present invention is a hydrocarbon-based anion exchange membrane in which an anion exchange resin is filled in a void portion of a porous membrane, and the ion exchange resin has an aromatic ring. The hydrocarbon-based anion exchange membrane is characterized in that a group having a plurality of anion exchange groups is bonded to the aromatic ring.

  In the present invention, the hydrocarbon-based anion exchange membrane is a hydrocarbon-based material in which a base material portion excluding a group having a plurality of anion exchange groups of an anion exchange resin, which is filled in a void portion of a porous membrane, is crosslinked. It is composed of a polymer. Here, the hydrocarbon polymer is a polymer which does not substantially contain a carbon-fluorine bond, and most of the main chain and side chain bonds constituting the polymer are carbon-carbon bonds. Say that. In other words, a small amount of other atoms such as oxygen, nitrogen, silicon, sulfur, boron, and phosphorus are interposed between the carbon-carbon bonds constituting the main chain and the side chain due to ether bonds, ester bonds, amide bonds, siloxane bonds, etc. You may do it.

  In addition, the atoms bonded to the main chain and the side chain need not all be hydrogen atoms, and if the amount is small, other atoms such as chlorine, bromine, fluorine, iodine, etc., or substituents containing other atoms It may be replaced. The amount of these elements other than carbon and hydrogen is preferably 40 mol% or less, preferably 10 mol% or less, based on all elements constituting the resin excluding the anion exchange group.

  In the hydrocarbon-based anion exchange membrane of the present invention, the anion exchange resin filled in the voids of the porous membrane has an aromatic ring.

  Such an anion exchange resin having an aromatic ring means that a monomer unit of a polymer chain of the anion exchange resin is formed by a chain of aromatic rings, or has an aromatic ring in a side chain. An anion exchange resin composed of a polymer formed from monomer units is exemplified. In particular, in the case of a monomer unit having an aromatic ring in the side chain, by using styrene or a styrene derivative as a polymerizable monomer when obtaining an anion exchange resin, the fragrance in the styrene or styrene derivative is obtained. It becomes easy to introduce a halogenoalkyl group as a substituent into the group ring, and furthermore, it becomes easy to introduce a group having a plurality of anion exchange groups.

  In the group having a plurality of anion exchange groups, the plurality of anion exchange groups are preferably a tertiary amino group or a quaternary ammonium group, and at least one is a quaternary ammonium group.

  Specifically, the anion exchange resin constituting the hydrocarbon-based anion membrane of the present invention is preferably an anion exchange resin having a skeleton represented by the general formula (1) or (2).

Here, in the general formulas (1) and (2), n and m are integers of 1 to 8, and R ¹ , R ² , R ³ , R ⁴ and R ⁵ are the same or different and have 1 to 4 carbon atoms. R ¹ and R ³ , R ² and R ⁴ may each form a ring, and X ⁻ is selected from a halogen ion, a hydroxide ion, a carbonate ion, and a bicarbonate ion. Anion.

n is preferably an integer of 1 to 4, and m is preferably an integer of 2 to 6. R ¹ , R ² , R ³ , R ⁴ , and R ⁵ are preferably a methyl group or an ethyl group. When R ¹ and R ³ , R ² and R ⁴ each form a ring, R ¹ and R ³ , R ² and R ⁴ form an ethylene chain, an n-propylene chain, and an n-butylene chain. Preferably, it is an ethylene chain. At this time, m is preferably an integer of 2 to 4, and more preferably 2.

  The anion exchange resin having a skeleton represented by the general formula (1) or (2) is composed of a polymer containing a repeating unit of a monocyclic aromatic polymerizable monomer having a main chain having a styrene skeleton. A group having a plurality of anion exchange groups is bonded to an aromatic ring. Further, in the group having a plurality of anion exchange groups, a quaternary ammonium group is bonded to the aromatic ring via an alkylene chain, and at least an alkyl group of the quaternary ammonium group bonded to the aromatic ring. Since one is a substituted alkyl group having a tertiary amino group or a quaternary ammonium group, it has a structure having a plurality of anion exchange groups for one side chain. In the skeleton represented by the general formula (1), the anion exchange group of the group having a plurality of anion exchange groups is a mixture of a tertiary amino group and a quaternary ammonium group, and is represented by the general formula (2). In the skeleton, the anion exchange group of a group having a plurality of anion exchange groups is a quaternary ammonium group.

  The anion exchange resin may have only a skeleton represented by the general formula (1) as a skeleton having an anion exchange group, but also has a skeleton represented by the general formula (2). It is preferable that 75 mol% of the anion exchange groups in the ion exchange membrane are quaternary ammonium groups.

  In such a hydrocarbon-based anion exchange membrane, the tertiary amino group is a weakly basic ion exchange group, which itself does not have anion exchange capacity, but increases the water content by increasing the ion exchange capacity, and the membrane The effect of reducing resistance is obtained. On the other hand, the quaternary ammonium group has an anion exchange ability, and an effect of increasing ionic conductivity is obtained. Therefore, when 75% or more of the ion exchange groups in the hydrocarbon-based anion exchange membrane are quaternary ammonium groups, the concentration of anions which are counterions of the anion exchange groups is high, and an anion having excellent ion conductivity. An ion exchange membrane can be preferably used.

  In addition to the skeleton represented by the general formula (1) or (2), the anion exchange resin constituting the hydrocarbon-based anion exchange membrane of the present invention increases the membrane density and increases the membrane strength. Furthermore, when used in a fuel cell or the like, a repeating unit of a crosslinkable polymerizable monomer such as divinylbenzene is also included in order to suppress a decrease in output due to permeation of fuel such as methanol.

  In addition, the said anion exchange resin may be mix | blended suitably with the other component in the range which does not impair the effect of this invention. In particular, in addition to the skeleton represented by the above general formula (1) or (2) and the repeating unit of the crosslinkable polymerizable monomer, styrene, acrylonitrile, methylstyrene, acrolein, methyl vinyl ketone, vinyl biphenyl as necessary. Other monomer repeating units, and plasticizers such as dibutyl phthalate, dioctyl phthalate, dimethyl isophthalate, dibutyl adipate, triethyl citrate, acetyl tributyl citrate, and dibutyl sebacate may be added.

  The porous membrane in which the anion exchange resin is filled in the voids is a membrane-like material having a number of pores having an average pore diameter of 0.005 to 5 μm and a thickness of 5 to 300 μm. At least a part of the pores communicate with the front and back so that an ion exchange membrane can be formed by being filled.

  As such a porous membrane, a polyolefin-based porous film is preferable. Among these, those made of polyethylene resin or propylene resin are preferred, and those made of polyethylene resin are most preferred.

  The hydrocarbon-based anion exchange membrane of the present invention is an anion exchange membrane precursor obtained by polymerizing after impregnating a polymerizable composition containing an aromatic polymerizable monomer having a halogenoalkyl group into a porous membrane. Is reacted with a polyamine to quaternize the halogenoalkyl group in the anion exchange membrane precursor into a quaternary ammonium group.

  In producing the hydrocarbon-based anion exchange membrane of the present invention, first, an anion exchange membrane precursor having a halogenoalkyl group is obtained. By reacting the obtained anion exchange membrane precursor with polyamine, the desired hydrocarbon-based anion exchange membrane can be obtained. Such an anion exchange membrane precursor can be obtained by impregnating a porous membrane with a polymerizable composition containing an aromatic polymerizable monomer having a halogenoalkyl group and then polymerizing. Polymerizable composition containing aromatic polymerizable monomer having halogenoalkyl group The polymerizable composition is (a) an aromatic polymerizable monomer having a halogenoalkyl group, and (b) a crosslinkable polymerizable monomer. And (c) a polymerization initiator, and may contain other components as necessary.

  In the method for producing a hydrocarbon-based anion exchange membrane, any known (a) aromatic polymerizable monomer having a halogenoalkyl group can be used without limitation. Examples of the halogenoalkyl group include chloromethyl group, bromomethyl group, iodomethyl group, chloroethyl group, bromoethyl group, iodoethyl group, chloropropyl group, bromopropyl group, iodopropyl group, chlorobutyl group, bromobutyl group, iodobutyl group, chloropentyl group, A bromopentyl group, an iodopentyl group, a chlorohexyl group, a bromohexyl group, and an iodohexyl group; Specific examples of such aromatic polymerizable monomers having a halogenoalkyl group include chloromethyl styrene, bromomethyl styrene, iodomethyl styrene, chloroethyl styrene, bromoethyl styrene, iodoethyl styrene, chloropropyl group, bromopropyl group. , Iodopropyl group, chlorobutyl group, bromobutyl group, iodobutyl group, chloropentyl styrene, bromopentyl styrene, iodopentyl styrene, chlorohexyl styrene, bromohexyl styrene, iodohexyl styrene, of which chloromethyl styrene, bromomethyl styrene , Iodomethyl styrene, chloroethyl styrene, bromoethyl styrene, iodoethyl styrene, chloropropyl styrene, bromopropyl styrene, iodopropyl styrene , Chlorobutyl styrene, bromobutyl styrene, to use iodine-butylstyrene, particularly preferred.

  In addition, the polymerizable composition used in the present invention is polymerized with an aromatic polymerizable monomer having a halogenoalkyl group to form a film-like material, thereby increasing the film density and increasing the film strength. Furthermore, when used in a fuel cell or the like, (b) a crosslinkable polymerizable monomer is also included for the purpose of suppressing a decrease in output due to permeation of fuel such as methanol.

  Such a crosslinkable polymerizable monomer is not particularly limited as long as it is a known monomer, and examples thereof include divinylbenzene, divinylsulfone, butadiene, chloroprene, divinylbiphenyl, divinylnaphthalene, diallylamine, and divinylpyridine. Divinyl compounds such as trivinylbenzene are used. These crosslinkable polymerizable monomers can be selected from a wide range as long as they are effective amounts necessary for maintaining the strength of the film and exhibiting the effect of preventing swelling and the like. However, the aromatic polymerizable monomer having a halogenoalkyl group can be used. When the ratio of the crosslinkable polymerizable monomer to the monomer is large, the ion exchange capacity of the obtained anion exchange membrane is decreased. On the contrary, when the ratio of the crosslinkable polymerizable monomer is small, the ion exchange capacity is reduced. The amount of the crosslinkable polymerizable monomer with respect to the aromatic polymerizable monomer having a halogenoalkyl group so that the obtained hydrocarbon-based anion exchange membrane has an ion exchange capacity suitable for the intended use. It is important to determine the proportion of the body. Generally, it is preferable to add 0.1 to 40 parts by weight, preferably 0.5 to 25 parts by weight with respect to 100 parts by weight of the aromatic polymerizable monomer having a halogenoalkyl group. When used as a diaphragm for a fuel cell, it is preferably 0.1 to 20 parts by mass, and preferably 0.1 to 15 parts by mass.

  Further, conventionally known polymerization initiators are used without any particular limitation. Specific examples of such polymerization initiators include octanoyl peroxide, lauroyl peroxide, t-butylperoxy-2-ethylhexanoate, benzoyl peroxide, t-butylperoxyisobutyrate, t-butylperoxy Organic peroxides such as laurate, t-hexyl peroxybenzoate, and di-t-butyl peroxide are used. In the polymerizable composition, the mixing ratio of these polymerization initiators can be selected from a wide range as long as it is an effective amount necessary for carrying out the polymerization reaction. Generally, aromatic polymerization having a halogenoalkyl group is performed. It is preferable to add 0.1 to 20 parts by mass, preferably 0.5 to 10 parts by mass with respect to 100 parts by mass of the polymerizable monomer.

  When an anion exchange membrane precursor is produced using a polymerizable composition containing an aromatic polymerizable monomer having a halogenoalkyl group, the polymerization is inhibited by hydrogen chloride gas or chlorine gas generated in the polymerization process. In order to prevent this, it is effective to add an epoxy compound as a compound scavenger to the polymerizable composition, and the mixing ratio thereof is a polymerizable composition 100 containing an aromatic polymerizable monomer having a halogenoalkyl group. It is preferable to set it as 1-12 mass parts with respect to a mass part, More preferably, it is 3-10 mass parts.

  As such a compound having an epoxy group (epoxy compound), a known compound having one or more epoxy groups in the molecule can be used without limitation. Specific examples include epoxidized vegetable oils such as epoxidized soybean oil and epoxidized linseed oil, derivatives thereof, terpene oxide, styrene oxide and derivatives thereof, epoxidized α-olefin, and epoxidized polymer. Such an epoxy compound can be obtained by the method described in JP-A No. 11-158486, or is commercially available (for example, ADEKA “ADEKA SIZER”, Kao “KABOX”, Kyoeisha Chemical “Epolite”, Daicel Chemical “Cyclo” "Mer" "Daimak", Nagase ChemteX "Denacol").

  In addition, other components can also be suitably mix | blended with the said polymeric composition in the range which does not impair the effect of this invention. In particular, in addition to the aromatic polymerizable monomer and the crosslinkable polymerizable monomer having the halogenoalkyl group, other monomers and plasticizers copolymerizable with these monomers as necessary. May be added. Examples of such other monomers include styrene, acrylonitrile, methylstyrene, acrolein, methyl vinyl ketone, and vinyl biphenyl. The blending ratio is 100 parts by mass or less, more preferably 80 parts by mass or less, more preferably 30 parts by mass with respect to 100 parts by mass of the polymerizable composition containing an aromatic polymerizable monomer having a halogenoalkyl group. Part or less.

  Further, as the plasticizers, dibutyl phthalate, dioctyl phthalate, dimethyl isophthalate, dibutyl adipate, triethyl citrate, acetyl tributyl citrate, dibutyl sebacate and the like are used. The blending ratio is preferably 50 parts by mass or less, more preferably 30 parts by mass or less with respect to 100 parts by mass of the polymerizable composition containing an aromatic polymerizable monomer having a halogenoalkyl group.

  The polymerizable composition having the above composition is polymerized after filling the voids of the porous membrane to obtain a hydrocarbon-based anion exchange membrane precursor. As such a porous membrane, any known base material of an ion exchange membrane may be used, and a porous film, non-woven paper, woven fabric, non-woven fabric, paper, inorganic membrane, etc. can be used without limitation, The material may also be a thermoplastic resin composition, a thermosetting resin composition, an inorganic material, or a mixture thereof, but it is easy to manufacture and has excellent mechanical strength, chemical stability, and chemical resistance. From the viewpoint of excellent and good compatibility with a hydrocarbon-based anion exchange resin, a polyolefin-based porous film is preferable.

  Specific examples of such polyolefin-based porous films include ethylene, propylene, 1-butene, 1-pentene, 1-hexene, 3-methyl-1-butene, 4-methyl-1-pentene, 5- What was manufactured with polyolefin resin, such as a homopolymer or copolymer of alpha olefins, such as methyl-1- heptene, is illustrated. Of these, those made of polyethylene or polypropylene resin are preferred, and those made of polyethylene resin are most preferred.

  By using a polyolefin-based porous film as the porous membrane, the physical strength of the anion exchange membrane can be increased without sacrificing electrical resistance because it functions as a reinforcing part of the obtained anion exchange membrane. It can be suitably used in the invention.

  Such a polyolefin-based porous film can be obtained, for example, by a method described in JP-A-9-216964, JP-A-2002-338721, or the like, or a commercially available product (for example, Asahi Kasei “Hypore”, Ube Industries “Yupor”, Tonen Tapils “Setera”, Nitto Denko “Exepor”, Mitsui Chemicals “Hilet”, etc.) are also available.

  The average pore diameter of the porous membrane is generally 0.005 to 5.0 μm and 0.01 to 1.0 μm in consideration of the small membrane resistance and mechanical strength of the obtained anion exchange membrane. More preferably, it is 0.015-0.4 micrometer. The porosity of the porous membrane is generally 20 to 95%, more preferably 30 to 80%, and most preferably 30 to 50% for the same reason as the average pore diameter. preferable.

  Furthermore, the film thickness of the porous film is generally selected from the range of 5 to 300 μm, and is preferably 5 to 60 μm from the viewpoint of obtaining a film having a smaller film resistance, and further has low methanol permeability. In consideration of providing balance and necessary mechanical strength, the thickness is most preferably 7 to 20 μm.

In the present invention, the average pore diameter of the porous membrane refers to a value measured by a half dry method in accordance with ASTM-F316-86. In addition, the porosity of the porous membrane is determined by the following formula, where the volume (Vcm ³ ) and mass (Ug) of the porous membrane are measured, and the density of the material of the porous membrane is X (g · cm ⁻³ ). The calculated value.

Porosity = [(V−U / X) / V] × 100 [%]
The method for filling the porous film with the polymerizable composition is not particularly limited. For example, a method of applying or spraying the polymerizable composition onto the porous film, or immersing the porous film in the polymerizable composition is exemplified. As a method for polymerizing the polymerizable composition filled in the voids of the porous membrane in this way into a hydrocarbon-based anion exchange membrane precursor, the porous membrane impregnated with the polymerizable composition is generally made of polyester or the like. A method of raising the temperature from room temperature under pressure is preferable. Such polymerization conditions depend on the type of polymerization initiator involved, the composition of the monomer composition, and the like, and are not particularly limited and may be appropriately selected.

  In addition, as a method for producing an anion exchange precursor, instead of an aromatic polymerizable monomer having a halogenoalkyl group, a polymerizable having a functional group capable of introducing a halogenoalkyl group such as styrene is used instead. It is also conceivable to use a monomer and polymerize the resin, and then introduce the halogenoalkyl group into a functional group capable of introducing the halogenoalkyl group. However, in this method, since the introduction reaction of the halogenoalkyl group proceeds from the surface of the film-like material, it is difficult to uniformly introduce the halogenoalkyl group in the film thickness direction, and the hydrocarbon-based anion obtained finally. The ion exchange capacity of the ion exchange membrane tends to be insufficient, resulting in an increase in membrane resistance. On the other hand, if excessive reaction conditions are used to introduce a halogenoalkyl group homogeneously throughout the membrane, the resin will decompose and the denseness will be lost. The ability of the membrane to inhibit fuel permeation becomes insufficient, making it difficult to produce a quaternary ammonium hydrocarbon anion exchange membrane suitable as the anion fuel cell membrane.

  In the hydrocarbon-based anion exchange membrane of the present invention, the anion exchange membrane precursor is further reacted with a polyamine to quaternize the halogenoalkyl group in the anion exchange membrane precursor into a quaternary ammonium group. Obtained by.

  Such a polyamine is a compound having two or more tertiary amino groups in a single molecule capable of reacting with a halogenoalkyl group to form a quaternary ammonium group, and any known compound can be used without limitation. Preferably, diamines, triamines, tetraamines, particularly preferably diamines are used. Such polyamines are represented by, for example, the following formulas (3) and (4).

In the formula, R ⁶ is a tetravalent hydrocarbon skeleton, preferably a hydrocarbon skeleton having 1 to 16 carbon atoms, and particularly preferably 2 to 6 carbon atoms. Also good. Y ¹ , Y ² , Y ³ and Y ⁴ are each independently —NR ⁷ R ⁸ (R ⁷ and R ⁸ are alkyl groups or —NR ⁹ R ¹⁰ (R ⁹ and R ¹⁰ are alkyl groups). Group), and at least two of Y ¹ , Y ² , Y ³ , and Y ⁴ are amino groups.

^{Z 1 -R 11 -Z 2 -R 12} -Z 3 -R 13 -Z 4 ··· (4)

In the formula, R ¹¹ , R ¹² and R ¹³ are a divalent hydrocarbon skeleton, preferably a hydrocarbon skeleton having 1 to 16 carbon atoms, particularly preferably 2 to 6 carbon atoms, It may be branched, and may be the same or different. Z ¹ and Z ⁴ are an amino group or hydrogen represented by —NR ¹⁴ R ¹⁵ (R ¹⁴ and R ¹⁵ are alkyl groups or amino groups represented by —NR ¹⁶ R ¹⁷ (where R ¹⁶ and R ¹⁷ are alkyl groups)). Z ² and Z ³ are each independently represented by —N (R ¹⁸ ) — (wherein R ¹⁸ is an alkyl group or an amino group represented by —NR ¹⁹ R ²⁰ (R ¹⁹ and R ²⁰ are alkyl groups)). And at least one of Z ¹ and Z ⁴ is an amino group.

In the above, when R ⁷ , R ⁸ , R ¹⁴ , R ¹⁵ and R ¹⁸ are alkyl groups, these are each independently an alkyl group having 1 to 4 carbon atoms, preferably a methyl group, an ethyl group, n- A propyl group, i-propyl group, n-butyl group, and i-butyl group are mentioned, More preferably, a methyl group and an ethyl group are mentioned.

R ⁹ , R ¹⁰ , R ¹⁶ , R ¹⁷ , R ¹⁹ and R ²⁰ are each independently an alkyl group having 1 to 4 carbon atoms, preferably a methyl group, an ethyl group, an n-propyl group, or an i-propyl group. , N-butyl group and i-butyl group, more preferably methyl group and ethyl group.

Among these, particularly preferred polyamines include N, N, N ′, N′-tetraalkylalkylenediamine compounds represented by the following general formula (5).

However, in the general formula (5), each of the substituents R ²¹ , R ²² , R ²³ , and R ²⁴ is independently an alkyl group having 1 to 4 carbon atoms, specifically, a methyl group, an ethyl group, n- A propyl group, i-propyl group, n-butyl group, and i-butyl group are mentioned, More preferably, a methyl group and an ethyl group are mentioned.

  Moreover, l is an integer of 1-8, More preferably, it is an integer of 2-6.

  In the production method of the present invention, the compound represented by the general formula (5) is not particularly limited. For example, N, N, N ′, N′-tetramethylethylenediamine, N, N, N ′ , N′-tetramethyl-1,3-propanediamine, N, N, N ′, N′-tetramethyl-1,4-butanediamine, N, N, N ′, N′-tetramethyl-1,5 -Pentanediamine, N, N, N ', N'-tetramethyl-1,6-hexanediamine, N, N, N', N'-tetraethylethylenediamine, N, N, N ', N'-tetraethyl-1 , 3-propanediamine, N, N, N ′, N′-tetraethyl-1,4-butanediamine, N, N, N ′, N′-tetraethyl-1,5-pentanediamine, N, N, N ′ , N′-tetraethyl-1,6-hexanediamine, etc. .

  Other than the compounds represented by the general formula (5) among the compounds represented by the general formula (3) or (4), for example, N, N, N ′, N ′, N ″, N ″ -Hexamethylmethanetriamine, N, N, N ', N', N ", N", N '' ', N' ''-octamethylmethanetetraamine, N, N, N ', N', N ″, N ″ -hexamethyl-1,1,2-ethanetriamine, N, N, N ′, N ′, N ″, N ″, N ′ ″, N ′ ″-octamethyl-1 , 1,2,2-ethanetetraamine, N, N, N ′, N ′, N ″, N ″ -hexamethyl-1,1,3-propanetriamine, N, N, N ′, N ′, N ″, N ″, N ″ ′, N ′ ″-octamethyl-1,1,3,3-propanetetraamine, N, N, N ′, N ′, N ″, N ″ — Hexamethyl 1,1,4-butanetriamine, N, N, N ′, N ′, N ″, N ″, N ′ ″, N ′ ″-octamethyl-1,1,4,4-butanetetraamine N, N, N ′, N ′, N ″, N ″ -hexamethyl-1,1,5-pentanetriamine, N, N, N ′, N ′, N ″, N ″, N ′ ″, N ″ ′-octamethyl-1,1,5,5-pentanetetraamine, N, N, N ′, N ′, N ″, N ″ -hexamethyl-1,1,6-hexanetriamine N, N, N ′, N ′, N ″, N ″, N ′ ″, N ′ ″-octamethyl-1,1,6,6-hexanetetraamine, N, N, N ′, N′-tetramethyl-1,2-propanediamine, N, N, N ′, N′-tetramethyl-1,3-butanediamine, N, N, N ′, N′-tetramethyl-1,4- Pentangi Min, N, N, N ′, N′-tetramethyl-1,5-hexanediamine, N, N, N ′, N′-tetraethyl-2,3-butanediamine, N, N, N ′, N ′ -Tetraethyl-2,4-pentanediamine, N, N, N ', N'-tetraethyl-2,5-hexanediamine, N, N, N', N'-tetraethyl-2,3-pentanediamine, N, N, N ′, N′-tetraethyl-2,3-hexanediamine, N, N, N ′, N′-tetraethyl-2,4-hexanediamine, 2,2′-bis (dimethylaminomethyl) propane, 1 , 1 ′, 1 ″ -tris (dimethylaminomethyl) ethane, tetrakis (dimethylaminomethyl) methane and the like.

  Moreover, in the said General formula (3) or (4), the alkyl groups which two amino groups which exist in a molecule | numerator may couple | bond together, and the ring may be formed as an alkylene chain.

  An example of such a compound is a cyclic compound represented by the following general formula (6).

  In General formula (6), p, q, and r are integers of 2-16, Preferably they are integers of 2-4, Comprising: These may be the same or different. Specific examples include an ethylene chain, an n-propylene chain, and an n-butylene chain, and an ethylene chain is more preferable. Among the compounds represented by the general formula (6), 1,4-diazabicyclo [2,2,2] octane is preferable.

  Among these compounds, N, N, N ′, N′-tetramethylethylenediamine, in terms of availability, reactivity with halogenoalkyl groups, and the effect of improving the water content of the resulting anion exchange membrane, N, N, N ′, N′-tetramethyl-1,3-propanediamine, N, N, N ′, N′-tetramethyl-1,4-butanediamine, N, N, N ′, N′— Tetramethyl-1,6-hexanediamine, N, N, N ′, N′-tetraethylethylenediamine, 1,4-diazabicyclo [2,2,2] octane and the like are more preferably used.

  In order to obtain the hydrocarbon-based anion exchange membrane of the present invention, it is important that one molecule of polyamine reacts with one halogenoalkyl group in the anion exchange membrane precursor. That is, only one of the plurality of tertiary amino groups of the polyamine is reacted with the halogenoalkyl group, and it is necessary to increase the molar ratio of the polyamine reacted with the halogenoalkyl group. The amount of the polyamine to be reacted with the halogenoalkyl group is 2 or more, preferably 7 or more in terms of the molar ratio of the polyamine to the halogenoalkyl group in the anion exchange membrane precursor.

  When the molar ratio of the polyamine to be reacted is low with respect to the total halogenoalkyl groups in the anion exchange membrane precursor, the halogenoalkyl groups in which a plurality of tertiary amino groups of one molecule of polyamine are contained in the anion exchange resin precursor The anion exchange capacity of the resulting anion exchange membrane does not increase.

  The reaction between the halogenoalkyl group in the anion exchange membrane precursor and the polyamine is preferably carried out in a solvent from the viewpoint of improving the familiarity between the anion exchange membrane precursor and the polyamine. Such a solvent is not particularly limited as long as it dissolves polyamine and a quaternary ammonium group forming reaction between the anion exchange membrane precursor and the polyamine proceeds. Examples of the organic solvent that can be suitably used include dichloroethane, chloroform, methanol, ethanol, 1-propanol, 2-propanol, methyl ethyl ketone, acetonitrile, nitromethane, tetrahydrofuran, dioxane, N, N-dimethylformamide, toluene and the like.

The concentration of the polyamine is not particularly limited, but may be suitably determined according to the combination of the solvent and the compound is preferably ^{1mmol · L -1 ~2mol · L -1} , 10mmol · L -1 ~2mol · L -1 Is particularly preferred. When the concentration of the polyamine is too low, the halogenoalkyl group and the polyamine do not easily come into contact with each other, and a plurality of tertiary amino groups of one molecule of the polyamine react with the halogenoalkyl group. It can no longer be obtained. When the concentration of polyamine is too high, the amount of the solvent for allowing the anion exchange membrane precursor and the polyamine to become compatible becomes relatively small, so that these compatibility becomes worse, and the quaternary ammonium group formation reaction is difficult to proceed. .

  The reaction temperature is 5 to 60 ° C., and the immersion time is about 0.5 to 72 hours. After the anion exchange membrane precursor and the polyamine are reacted, washing may be performed for the purpose of removing excess polyamine that has not been subjected to the reaction, and it may or may not be dried thereafter.

  The anion exchange group possessed by the hydrocarbon-based anion exchange membrane obtained by the above-described method includes a quaternary ammonium group formed by a reaction between a polyamine and a halogenoalkyl group, and a plurality of tertiary amino groups possessed by the polyamine. Although it is a mixture with a tertiary amino group that has not been used for the reaction with a halogenoalkyl group, particularly when used as a diaphragm for an anionic fuel cell, the tertiary amino group is converted to a quaternary ammonium group. From the viewpoint of improving the anion conductivity, it is preferable to use a hydrocarbon-based anion exchange membrane in which 75 mol% or more of the anion exchange groups are quaternary ammonium groups having anion exchange ability.

A hydrocarbon ion exchange membrane in which a tertiary amino group is converted to a quaternary ammonium group can be obtained by quaternizing the tertiary amino group with a halogenoalkane. The method of quaternization may be in accordance with a conventional method. More specifically, the quaternization is performed by immersing the hydrocarbon-based anion exchange membrane in a solution containing a halogenoalkane such as methyl iodide or ethyl iodide. The concentration of the halogenoalkane solution is not particularly limited, and is about 0.1 to 2 mol·L ⁻¹ , the immersion temperature is 5 to 60 ° C., and the immersion time is about 0.5 to 24 hours.

  The hydrocarbon-based anion exchange membrane obtained by the above production method usually has a halogeno ion as a counter ion of a quaternary ammonium group, but when the anion exchange membrane is used as an anion-type fuel cell membrane, the fuel cell It is particularly preferable to exchange the counter ion of the quaternary ammonium group with a hydroxide ion that becomes a mobile ion in the membrane in terms of easy output, and carbonic acid that can be easily replaced with a hydroxide ion by a catalytic reaction during fuel cell power generation. It is also preferred to ion exchange to ions or bicarbonate ions.

  This ion exchange method may be in accordance with a conventional method, and when ion exchange to hydroxide ions is performed, the anion exchange membrane is immersed in an aqueous alkali hydroxide solution such as an aqueous sodium hydroxide solution or an aqueous potassium hydroxide solution. . The concentration of the alkali hydroxide aqueous solution is not particularly limited, and is about 0.1 to 2 mol / L, the immersion temperature is 5 to 60 ° C., and the immersion time is about 0.5 to 24 hours. In addition, ion exchange to carbonate ions or bicarbonate ions can be achieved quickly by absorbing carbon dioxide in the air even if the membrane ion-exchanged to hydroxide ions is left in the air (usually water The change of the counter ion from the acid ion to the bicarbonate ion is a rate at which about 90% or more of the substitution is completed in 10 hours at room temperature and in the atmosphere), but the aqueous solution of sodium carbonate, aqueous solution of sodium bicarbonate, aqueous solution of potassium carbonate, It can also carry out without passing through the ion exchange to a hydroxide ion by immersing in alkaline carbonate water, such as potassium bicarbonate, or an alkaline bicarbonate solution. At that time, the concentration of the alkali carbonate aqueous solution and the alkali bicarbonate aqueous solution is not particularly limited, and is about 0.1 to 2 mol / L, the immersion temperature is 5 to 60 ° C., and the immersion time is 0.5 to 24 hours. Degree.

  According to the production method described above, it is possible to produce a hydrocarbon-based anion exchange membrane having a high water content, a low membrane resistance, and an excellent ion conductivity, and this membrane also has a high mechanical strength. That is, even if the hydrocarbon-based anion exchange membrane of the present invention is made as thin as 5 μm, its burst strength is usually 0.08 MPa or more. Due to such high burst strength, cracks occur when an anion exchange membrane is incorporated into a fuel cell, or pinholes are generated by carbon paper fibers normally used as gas diffusion electrodes. This can be suppressed. Furthermore, the burst strength can be increased to 0.1 MPa or more by increasing the film thickness of the porous film or increasing the amount of the crosslinkable polymerizable monomer to a suitable range. It is also possible to manufacture up to 1.0 MPa.

  Such an anion exchange membrane is particularly suitably used as a diaphragm for electrochemical devices such as an anionic fuel cell, an electrochemical gas sensor, an electrochemical air cleaner, and an electrochemical dehumidifier.

When the hydrocarbon-based anion exchange membrane of the present invention is used as a diaphragm for an anionic fuel cell, the total ion exchange capacity of the anion exchange membrane is preferably 2.0 to 5.0 mmol · g ^−1. Most preferably, it is 5-5.0 mmol · g ⁻¹ .

  In the anion exchange membrane B, the ratio of the quaternary ammonium group to the total ion exchange capacity (also referred to as quaternization rate) is preferably 75% or more, more preferably 90% or more, and 95 % Or more is most preferable.

The membrane resistance of the anion exchange membrane is preferably 0.005 to 1.2 Ω · cm ² as measured in a 0.5 mol·L ⁻¹ -NaCl aqueous solution at 25 ° C. Most preferably, it is 6 Ω · cm ² .

Here, it is practically difficult to reduce the film resistance to less than 0.005 Ω · cm ² . On the other hand, when the film resistance exceeds 1.2 Ω · cm ² , the electric resistance is too high to obtain a high battery output.

In the hydrocarbon-based anion exchange membrane, the anion conductivity when the counter ion of the anion exchange group is bicarbonate ion is 8.0 × 10 ⁻³ S as measured by the AC impedance method at 40 ° C. It is preferably cm ⁻¹ or more, and more preferably 1.0 × 10 ⁻² S · cm ⁻¹ or more.

  The produced hydrocarbon-based anion exchange membrane is washed and cut as necessary, and is used as a diaphragm for an anion exchange type fuel cell according to a conventional method.

  As the anion exchange type fuel cell employing the membrane of the present invention, the one having the basic structure shown in FIG. 1 is generally used, but of course, the present invention is also applied to anion type fuel cells having other known structures. be able to. As the fuel, hydrogen or methanol is the most common, and the effect of the present invention is most prominent. In addition, ethanol, ethylene glycol, dimethyl ether, ammonia, hydrazine, etc. have the same excellent effect. Is demonstrated.

  Hereinafter, examples will be given to describe the present invention in more detail, but the present invention is not limited to these examples.

  In addition, the measurement methods of anion exchange capacity, moisture content, membrane resistance, methanol permeability, mechanical strength, and fuel cell output voltage used for evaluating the characteristics of hydrocarbon-based anion exchange membranes in Examples and Comparative Examples are described below. .

1) Anion exchange capacity, quaternization rate, water content Anion exchange membrane is immersed in 0.5 mol·L ⁻¹ -HCl aqueous solution for 10 hours or more to quaternize tertiary amino groups and chloride ions. Type anion exchange membrane, then substituted with 0.2 mol·L ⁻¹ -NaNO ₃ aqueous solution to nitrate ion type, and released chloride ions using silver nitrate aqueous solution, potentiometric titrator (COMMITE-900, Hiranuma Sangyo Co., Ltd.) (Amol).

Then, the chloride ion type again immersed the same ion-exchange membrane to 1 mol ^· L -1-HCl aqueous solution, further, a 0.05 mol ^· L -1 -NaOH aqueous ^{solution, 4 mol} · L -1 -NaCl aqueous solution Quaternary ammonium that was immersed in a 1: 1 mixed solution for 16 hours or longer to neutralize protons on the tertiary amino group, and then substituted with a 0.2 mol·L ⁻¹ -NaNO ₃ aqueous solution to form a nitrate ion type. Group-derived chloride ions were quantified with a potentiometric titrator using an aqueous silver nitrate solution (Bmol).

Next, the same ion exchange membrane is immersed in a 0.5 mol·L ⁻¹ -NaCl aqueous solution at 25 ° C. for 4 hours or more, washed thoroughly with ion exchange water, taken out of the membrane, wiped with moisture on the surface with tissue paper, etc. The time weight (Wg) was measured. Further, the membrane was dried under reduced pressure at 60 ° C. for 5 hours and its weight was measured (Dg). Based on the above measured values, the ion exchange capacity, quaternization rate and water content were determined by the following equations.

Total anion exchange capacity = A × 1000 / D [mmol · g ⁻¹ -dry weight]
Quaternization rate = B / A × 100 [mol%]
Moisture content = 100 × (WD) / D [mass%]

2) Carbonate and bicarbonate ion concentration measurement of hydrocarbon-based anion exchange membrane First, 1.0 g of a hydrocarbon-based anion exchange membrane was immersed in 100 ml of 1 mol / L-NaCl aqueous solution for 30 minutes, and then the resulting immersion liquid was obtained. Is titrated with a 0.1 mol / L-phenolphthalein / ethanol solution, and the titer with the end point when red becomes colorless is defined as V1 ml. By this titration, neutralization of OH ⁻ ions and change of CO ₃ ²⁻ ions to HCO ₃ ⁻ ions are measured. Subsequently, this immersion liquid is titrated with a 0.1 mol / L-bromocresol green / methyl red mixed ethanol solution, and the titer with the end point when the color changes from green to orange is set to V2 ml. By this titration, the change in H ₂ CO ₃ of HCO ₃ ⁻ ions is measured.

From the relationship of pKa, when OH ⁻ ions and HCO ₃ ⁻ ions coexist, either one of the ions becomes a negligible amount that can be ignored. The concentrations of OH ⁻ ions, CO ₃ ²⁻ ions, and HCO ₃ ⁻ ions therein are calculated as follows when the titration amounts V1 and V2 have the following relationships, respectively.

When V1> V2: only OH ⁻ ions and CO ₃ ^2- ions are present as ion species.

0.1 × V2 [ml] × 10 ⁻³ / membrane weight [g]
= CO ₃ ^2- ion concentration [mmol / g]
0.1 × (V1-V2) [ml] × 10 ⁻³ / membrane weight [g]
= OH ^- ion concentration [mmol / g]

When V1 <V2: Only CO ₃ ²⁻ ions and HCO ₃ ⁻ ions are present as ion species.

0.1 × V1 [ml] × 10 ⁻³ / membrane weight [g]
= CO ₃ ^2- ion concentration [mmol / g]
0.1 × (V2-V1) [ml] × 10 ⁻³ / membrane weight [g]
= HCO ₃ ^- ion concentration [mmol / g]

When V1 = V2: only ionic species is CO ₃ ^2- ion.

0.1 × V1 [ml] × 10 ⁻³ / membrane weight [g]
= CO ₃ ^2- ion concentration [mmol / g]

3) Membrane resistance First, an anion exchange membrane was immersed in a 0.5 mol·L ⁻¹ -NaCl aqueous solution at 25 ° C. for 4 hours or more to perform ion exchange to obtain a chloride ion type anion exchange membrane, followed by platinum. The anion exchange membrane is placed in the center of a two-chamber cell equipped with electrodes, filled with 0.5 mol·L ⁻¹ -NaCl aqueous solution on both sides of the anion exchange membrane, and 25 ° C. by an AC bridge (frequency 1000 cycles / second). The resistance between the electrodes was measured. Similarly, the resistance between the electrodes was measured without installing an anion exchange membrane, and the membrane resistance was determined from the difference in resistance between the electrodes when a diaphragm was installed.

Electrical resistance = 1000 × (ab) / 100 [Ω · cm ² ]

4) Evaluation of anion conductivity Anion-exchange membranes left in the atmosphere for 24 hours or more in the air are moistened with ion-exchange water at 40 ° C. and then cut into strips approximately 6 cm wide and 2.0 cm long. An anion exchange membrane was prepared. Next, five platinum wires having a line width of 0.3 mm were arranged in the horizontal direction (same direction as the horizontal direction of the anion exchange membrane) at intervals of 0.5 cm, both parallel to each other and the vertical direction (vertical direction of the anion exchange membrane). An insulating substrate arranged in a straight line parallel to the same direction as the direction was prepared, and a measurement sample was prepared by pressing the platinum wire of the insulating substrate against the anion exchange membrane.
Between the first and second platinum wires (platinum wire spacing = 0.5 cm), between the first and third platinum wires (platinum wire spacing = 1.0 cm), the first and fourth wires The AC impedance was measured between the platinum wires (platinum wire spacing = 1.5 cm) and between the first and fifth platinum wires (platinum wire spacing = 2.0 cm). The resistance-to-resistance gradient (R) is obtained from a graph obtained by plotting each measured value with the distance between platinum wires on the x-axis and the AC impedance on the y-axis, and the anion conductivity (σ ) At this time, the AC impedance is such that the measurement sample is kept in a constant temperature and humidity chamber of 40 ° C. and 90% RH in a state where water droplets of ion exchange water are present on the surface of the anion exchange membrane, and an alternating current of 1 kHz between the platinum wires. It was measured as an alternating current impedance when. The film thickness (L) was measured by wetting the anion exchange membrane with ion exchange water.

δ = 1 / R × 2.0 × L
δ: conductivity [S · cm ⁻¹ ]
L: Film thickness [cm]
R: resistance-to-resistance gradient [Ω · cm ⁻¹ ]
In the graph above, a linear relationship (proportional relationship) is established between the distance between the platinum wires and the AC impedance, and the resistance due to contact (contact resistance) between the platinum wire and the anion exchange membrane in the measurement sample. Is evaluated as a y-intercept, and the slope (R) between the resistance electrodes, which means the specific resistance of the film, can be calculated from the slope of the graph. In this measurement, since the anion conductivity (σ) is obtained based on the resistance-to-resistance gradient (R), the influence of the contact resistance is eliminated.

5) Fuel cell output voltage A chloromethylstyrene-styrene copolymer having a molecular weight of 30,000 and a styrene content of 60% by weight is quaternized with trimethylamine, and then suspended in a large excess of 0.5 mol·L ⁻¹ -NaOH aqueous solution. A mixture of a tetrahydrofuran solution of an anion exchange resin (resin concentration: 5% by weight), which is turbid and ion-exchanged to hydroxide ions, and platinum and a carbon black supported by 50% by weight of a ruthenium alloy catalyst (ruthenium 50 mol%) are mixed with polytetra The catalyst was applied to carbon paper having a thickness of 100 μm and a porosity of 80% treated with fluoroethylene to make the catalyst 2 mg · cm ⁻² and dried under reduced pressure at 80 ° C. for 4 hours to obtain a gas diffusion electrode. .

Next, the above gas diffusion electrodes were set on both surfaces of the anion exchange membrane to be measured, and hot-pressed for 100 seconds under a pressure of 100 ° C. and a pressure of 5 MPa, and then allowed to stand at room temperature for 2 minutes. This was incorporated into a fuel cell having the structure shown in FIG. 1 and the temperature of the fuel cell was set to 50 ° C., a 10 wt% methanol aqueous solution on the fuel electrode side, and atmospheric pressure oxygen on the oxidation electrode side at 200 ml · min. ^The power generation test was repeated until the output was stabilized after being supplied at ⁻¹ , and the cell terminal voltages at current densities of 0 A · cm ⁻² and 0.1 A · cm ⁻² were measured.

(Examples 1-5)
First, 100 parts by mass of chloromethylstyrene, 10 parts by mass of 57% -divinylbenzene, 5 parts by mass of a polymerization initiator (trade name: perbutyl O), and 5 parts by mass of an epoxy compound (trade name: Epolite 40E) are mixed to be polymerizable. A monomer composition was obtained. 400 g of the obtained polymerizable composition was put into a 500 ml glass container, and a porous film having a size of 20 × 20 cm (made of polyethylene having a weight average molecular weight of 250,000, a film thickness of 25 μm, an average pore diameter of 0 in the polymerizable composition). 0.03 μm, porosity 37%) was immersed.

Subsequently, this porous membrane was taken out from the polymerizable composition, and both sides of the porous membrane were coated using a 100 μm polyester film as a release material, and then heated and polymerized at 80 ° C. for 5 hours under a nitrogen pressure of 0.3 MPa. An anion exchange membrane precursor was obtained. As a result of elemental analysis, the amount of chlorine in the anion exchange membrane precursor is 0.18 mg · cm ⁻² , and the number of moles of halogenoalkyl groups contained in the anion exchange membrane precursor having a size of 20 × 20 cm is Calculated as 2.0 mmol.

This anion exchange membrane precursor is immersed in 100 ml of an aqueous solution containing a predetermined concentration of polyamine and 25% by weight of acetone shown in Table 1 for 48 hours at room temperature to introduce anion exchange groups, and an anion exchange membrane is obtained. Obtained. Subsequently, it was suspended in a large excess of 0.5 mol·L ⁻¹ -NaOH aqueous solution, and the counter ion was ion exchanged from chloride ion to hydroxide ion to obtain a hydroxide ion type hydrocarbon anion exchange membrane.

  The anion exchange capacity, water content, membrane resistance, anion conductivity, film thickness, and fuel cell output voltage of these anion exchange membranes were measured. The results are shown in Table 2.

(Examples 6 to 10)
The anion exchange membranes obtained in Examples 1 to 5 were immersed in 100 ml of an acetone solution containing 40% by weight of methyl iodide at room temperature for 24 hours, and the remaining tertiary amine groups derived from polyamine were quaternized. After quaternization to an ammonium group, it is suspended in a large excess of 0.5 mol·L ⁻¹ -NaOH aqueous solution, and the counter ion is ion-exchanged from a chloride ion to a hydroxide ion. An anion exchange membrane for a battery was obtained.

  The anion exchange capacity, water content, membrane resistance, anion conductivity, film thickness, and fuel cell output voltage of these fuel cell diaphragms were measured. The results are shown in Table 2.

(Example 11)
In Example 8, instead of ^{0.5 mol} · L -1 -NaOH aqueous solution, using a large excess of ^0.5mol · L -1 -NaHCO ₃ solution, ion-exchanged counter ion from chloride ion to bicarbonate ions After that, the same operation as in Example 8 was performed.

  The anion exchange capacity, water content, membrane resistance, ion conductivity, film thickness, and fuel cell output voltage of the obtained fuel cell membrane were measured. The results are shown in Table 2.

(Comparative Examples 1 and 2)
An anion exchange membrane was obtained by performing the same operation as in Example 1 except that trimethylamine was used instead of the polyamine shown in Example 1 (Comparative Example 1). Subsequently, the same operation as Example 6 was performed about this anion exchange membrane, and the anion exchange membrane was obtained (comparative example 2).

  The anion exchange capacity, water content, membrane resistance, anion conductivity, and fuel cell output voltage of this anion exchange membrane were measured. The results are shown in Table 2.

(Comparative Examples 3-6)
The same operation as in Example 1 was carried out except that the polyamine having a predetermined concentration shown in Table 1 was used to obtain a fuel cell diaphragm (Comparative Examples 3 and 4). Subsequently, operation similar to Example 6 was performed about each anion exchange membrane, and the anion exchange membrane was obtained (comparative examples 5 and 6).

  The anion exchange capacity, water content, membrane resistance, anion conductivity, and fuel cell output voltage of the fuel cell membrane were measured. The results are shown in Table 2.

It is a conceptual diagram which shows the basic structure of a polymer electrolyte fuel cell.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1; Battery partition wall 2; Fuel gas flow hole 3; Oxidant gas flow hole 4; Fuel chamber side gas diffusion electrode 5; Oxidant chamber side gas diffusion electrode 6; Solid polymer electrolyte (anion exchange membrane)
7; Fuel chamber 8; Oxidant chamber

Claims (9)

A hydrocarbon-based anion exchange membrane in which a void portion of a porous membrane is filled with an ion exchange resin, the ion exchange resin having an aromatic ring, and an anion exchange group on the aromatic ring A hydrocarbon-based anion exchange membrane formed by bonding a plurality of groups. 2. The anion exchange membrane according to claim 1, wherein the anion exchange group in the group having a plurality of anion exchange groups is a tertiary amino group or a quaternary ammonium group, and at least one is a quaternary ammonium group. A hydrocarbon-based anion exchange membrane. The anion exchange membrane according to claim 2, wherein 75 mol% or more of the ion exchange groups are quaternary ammonium groups. The anion exchange resin having an aromatic ring according to claim 1 is an anion exchange resin comprising a polymer containing a repeating unit of a monocyclic aromatic polymerizable monomer having a styrene skeleton. A hydrocarbon-based anion exchange membrane formed by bonding a group having a plurality of anion exchange groups to a ring. A hydrocarbon-based anion exchange membrane comprising an anion exchange resin having a skeleton represented by general formula (1) or (2), wherein the anion exchange membrane according to claim 2 or 4.

In the general formulas (1) and (2), n and m are integers of 1 to 8, and R ¹ , R ² , R ³ , R ⁴ , and R ⁵ may be the same or different and have 1 to 4 carbon atoms. A good alkyl group, R ¹ and R ³ , R ² and R ⁴ may each form a ring, and X ⁻ is an anion selected from a halogen ion, a hydroxide ion, a carbonate ion, and a bicarbonate ion Indicates. The anion-type fuel cell membrane comprising an anion exchange membrane according to claim 1, wherein the counter ion of the anion exchange group is an anion selected from hydroxide ion, carbonate ion and bicarbonate ion. 2. An anion exchange membrane precursor obtained by polymerizing a porous film after impregnating a polymerizable composition containing an aromatic polymerizable monomer having a halogenoalkyl group with a polyamine. 2. A method for producing a hydrocarbon-based anion exchange membrane according to 1. The method for producing an anion exchange membrane according to claim 7, wherein the molar ratio of the polyamine to the halogenoalkyl group in the reaction of the halogenoalkyl group in the anion exchange membrane precursor with the polyamine is 2 or more. An anion exchange membrane precursor having a halogenoalkyl group obtained from a polymerizable composition containing a monocyclic aromatic polymerizable monomer is reacted with a polyamine, and then the remaining tertiary amino group is reacted with a halogenoalkane. The method according to claim 7, wherein the tertiary amino group is converted to a quaternary ammonium group.

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