Patent Application
20090317684
The present invention relates to a polymer electrolyte membrane. More specifically, the present invention relates to a polymer electrolyte membrane which is used as an electrolyte membrane for a solid polymer type fuel cell.
A solid polymer type fuel cell is a power generator for generating electricity by a chemical reaction between hydrogen and oxygen, and the use thereof is very expected for generation of one of next-generation energies in the fields of electrical machinery industry and automobile industry. In place of a fluorine-based polymer electrolyte typified by Nafion (registered trademark of E. I. du Pont de Nemours and Company) which has conventionally been used as a diaphragm in the solid polymer type fuel cell, a hydrocarbon-based polymer electrolyte having excellent heat resistance and gas barrier properties has attracted special interest recently (JP-A No. 6-93114).
To industrially produce a hydrocarbon-based polymer electrolyte membrane, it is important to continuously forming a membrane while maintaining high characteristics and high quality. For example, a membrane is usually formed by a so-called solution casting method in which an aromatic polymer electrolyte is dissolved in a solvent and the resulting solution is applied by flow casting and then dried (JP-A No. 2003-031232, JP-A No. 2004-134225, JP-A No. 2005-154710, JP-A No. 2005-216525).
In the solution casting method associated with the process for production of a polymer electrolyte membrane for a solid polymer type fuel cell, a membrane is produced through the steps of applying a solution on a supporting substrate, drying a solvent and removing the solvent by immersion in water, followed by dehydration. In the process in which a membrane is produced through these complicated steps, it is required to continuously produce a polymer electrolyte membrane from an industrial point of view. Therefore, it is considered to be important that it is easy to handle the resulting polymer electrolyte membrane. For example, it is important that properties of both surfaces of the polymer electrolyte membrane are almost the same and both surfaces can be handled in the same way.
In the step of producing a membrane-electrode assembly by attaching an electrode to both surfaces of the polymer electrolyte membrane thus obtained, bondability at an interface between a membrane and an electrode, and thus a polymer electrolyte membrane whose both surfaces have surface properties having high affinity with the electrode is important.
In light of industrial production of a polymer electrolyte membrane for a solid polymer type fuel cell, an object of the present invention is to provide a polymer electrolyte membrane in which it is easy to handle during a continuous step and also bondability at the interface between a membrane and an electrode enhances in the production process of a membrane-electrode assembly.
The present inventors have intensively studied so as to achieve the above-described object, and thus the present invention has been completed. The present invention provides an ion conductive polymer electrolyte membrane, a laminate comprising the polymer electrolyte membrane, and a method for producing the same.
First, the present invention provides a method for producing a laminate according to the following [1].
[1] A method for producing a laminate, wherein an ion conductive polymer electrolyte membrane is laminated on a supporting substrate in a state where any one surface of the polymer electrolyte membrane is bonded to the supporting substrate, a difference in a contact angle against water between one surface and the other surface of the ion conductive polymer electrolyte membrane being 30° or less, the method comprising the steps of:
preparing a polymer electrolyte solution obtained by dissolving a polymer electrolyte containing an ion conductive polymer having an aromatic group in the main chain and/or the side chain, and also having an ion exchange group bonded directly to the aromatic group or bonded indirectly to the aromatic group via the other atom or atomic group in a solvent; and
applying the polymer electrolyte solution on the supporting substrate by flow casting thereby laminating the polymer electrolyte membrane on the supporting substrate.
Furthermore, the present invention provides the following [2] and [3] as preferred embodiments according to the above-described [1].
[2] The method for producing a laminate according to [1], wherein the surface to be coated by flow casting of the supporting substrate is formed of a metal or a metal oxide.
[3] The method for producing a laminate according to [1] or [2], wherein the supporting substrate is a continuous supporting substrate which is a film containing a metal or a metal oxide on the surface.
A supporting substrate whose surface to be coated by flow casting is formed of a metal or metal oxide is suited as a supporting substrate in which a contact angle against water of both surfaces of the polymer electrolyte membrane can be easily decreased by application through flow casting. From the viewpoint of industrial use, a film containing a metal or metal oxide on the surface is used as a continuous supporting substrate.
The present invention provides the following [4] to [15] in any one of the above-described methods.
[4] The method for producing a laminate according to any one of [1] to [3], wherein the ion conductive polymer has an aromatic ring in the main chain, and also has an ion exchange group bonded directly to the aromatic group or bonded indirectly to the aromatic group via the other atom or atomic group.
[5] The method for producing a laminate according to [4], wherein the ion conductive polymer has a side chain.
[6] The method for producing a laminate according to any one of [1] to [3], wherein the ion conductive polymer has an aromatic ring in the main chain, and also may have the side chain having an aromatic ring and has an ion exchange group in which at least one of the aromatic ring of the main chain and the aromatic ring of the side chain is bonded directly to the aromatic ring.
[7] The method for producing a laminate according to any one of [4] to [6], wherein the ion exchange group is a sulfonic acid group.
[8] The method for producing a laminate according to any one of [1] to [7], wherein the ion conductive polymer has one or more repeating units having an ion exchange group selected from the following general formulas (1a) to (4a):
wherein Ar1 to Ar9 each independently represents a divalent aromatic group which has an aromatic ring in the main chain and may also have a side chain having an aromatic ring, having an ion exchange group in which at least one of the aromatic ring of the main chain and the aromatic ring of the side chain is bonded directly to the aromatic ring, Z and Z′ each independently represents either CO or SO2, X, X′ and X″ each independently represents either O or S, Y represents a direct bond or a group represented by the following general formula (10), p′ represents 0, 1 or 2, and q and r each independently represents 1, 2 or 3; and one or more repeating units having substantially no ion exchange group selected from the following general formulas (1b) to (4b):
wherein Ar11 to Ar19 each independently represents a divalent aromatic group which may have a substituent as the side chain, Z and Z′ each independently represents either CO or SO2, X, X′ and X″ each independently represents either O or S, Y represents a direct bond or a group represented by the following general formula (10), p′ represents 0, 1 or 2, and q′ and r′ each independently represents 1, 2 or 3, and
wherein R1 and R2 each independently represents a hydrogen atom, an alkyl group having 1 to 10 carbon atoms which may have a substituent, an alkoxy group having 1 to 10 carbon atoms which may have a substituent, an aryl group having 6 to 18 carbon atoms which may have a substituent, an aryloxy group having 6 to 18 carbon atoms which may have a substituent, or an acyl group having 2 to 20 carbon atoms which may have a substituent, and R1 and R2 may be combined to form a ring.
[9] The method for producing a laminate according to any one of [1] to [8], wherein the ion conductive polymer is a copolymer having one or more polymer segments (A) having an ion exchange group, and one or more polymer segments (B) having substantially no ion exchange group.
[10] The method for producing a laminate according to any one of [1] to [9], wherein the ion conductive polymer is a block copolymer comprising a block (A) having an ion exchange group and a block (B) having substantially no ion exchange group.
[11] The method for producing a laminate according to any one of [1] to [10], capable of forming a polymer electrolyte membrane having a structure microphase-separated into at least two or more phases.
[12] The method for producing a laminate according to any one of [1] to [11], capable of forming a polymer electrolyte membrane which contains, as the ion conductive polymer, a block copolymer comprising a block (A) having an ion exchange group and a block (B) having substantially no ion exchange group, and also has a microphase-separated structure containing a phase having a high density of a block (A) having an ion exchange group and a phase having a high density of a block (B) having substantially no ion exchange group.
[13] The method for producing a laminate according to any one of [1] to [12], wherein the ion conductive polymer has at least one block (A) having an ion exchange group and at least one block (B) having substantially no ion exchange group, the block (A) having an ion exchange group has a repeating unit represented by the following general formula (4a′):
wherein m represents an integer of 5 or more, Ar9 represents a divalent aromatic group, in which the divalent aromatic group may be substituted with a fluorine atom, an alkyl group having 1 to 10 carbon atoms which may have a substituent, an alkoxy group having 1 to 10 carbon atoms which may have a substituent, an aryl group having 6 to 18 carbon atoms which may have a substituent, an aryloxy group having 6 to 18 carbon atoms which may have a substituent or an acyl group having 2 to 20 carbon atoms which may have a substituent, and Ar9 has an ion exchange group bonded directly to an aromatic ring constituting the main chain or bonded indirectly to the aromatic ring via the side chain, and also the block (B) having substantially no ion exchange group has one or more repeating structures selected from the following general formulas (1b′), (2b′) and (3b′):
wherein n represents an integer of 5 or more, Ar11 to Ar18 each independently represents a divalent aromatic group, in which the divalent aromatic group may be substituted with an alkyl group having 1 to 18 carbon atoms, an alkoxy group having 1 to 10 carbon atoms, an aryl group having 6 to 10 carbon atoms, an aryloxy group having 6 to 18 carbon atoms or an acyl group having 2 to 20 carbon atoms, and other symbols are the same as those in the general formulas (1b) to (3b).
[14] The method for producing a laminate according to any one of [1] to [13], wherein the ion conductive polymer has at least one block (A) having an ion exchange group and at least one block (B) having substantially no ion exchange group, and also the ion exchange group is directly bonded to the aromatic ring of the main chain in the block (A) having an ion exchange group.
[15] The method for producing a laminate according to any one of [1] to [14], wherein the ion conductive polymer has at least one block (A) having an ion exchange group and at least one block (B) having substantially no ion exchange group, and also both the block (A) having an ion exchange group and the block (B) having substantially no ion exchange group substantially have no substituent containing a halogen atom.
The present invention also provides the following [16] to [37] by any one of the above-described methods.
[16] A method for producing a polymer electrolyte membrane, comprising the step of removing the supporting substrate from the laminate obtained by the method according to any one of [1] to [15].
[17] The method for producing a polymer electrolyte membrane according to [16], which does not comprise the step of surface-treating the both surface of the polymer electrolyte membrane after removing the supporting substrate.
[18] A laminate obtained by the method according to any one of [1] to [15].
[19] A polymer electrolyte membrane obtained by the method according to [16] or [17].
[20] A ion conductive polymer electrolyte membrane containing at least one ion conductive polymer, wherein at least any one surface of the polymer electrolyte membrane is not subjected to the surface treatment, and also a difference in a contact angle against water between one surface and the other one surface of the polymer electrolyte membrane is 30° or less.
[21] The ion conductive polymer electrolyte membrane according to [20], wherein both surfaces of the polymer electrolyte membrane are not subjected to a surface treatment.
[22] The polymer electrolyte membrane according to [20] or [21], wherein the contact angle against water of both one surface and the other one surface of the membrane is 10° or more and 60° or less.
[23] The polymer electrolyte membrane according to any one of [20] to [22], wherein the ion conductive polymer has an aromatic ring in the main chain, and also has an ion exchange group bonded directly to the aromatic ring or bonded indirectly to the aromatic ring via the other atom or atomic group.
[24] The polymer electrolyte membrane according to [23], wherein the ion conductive polymer has a side chain.
[25] The polymer electrolyte membrane according to any one of [20] to [22], wherein the ion conductive polymer has an aromatic ring in the main chain, and also may have a side chain having an aromatic ring and has an ion exchange group in which at least one of the aromatic ring of the main chain or the aromatic ring of the side chain is bonded directly to the aromatic ring.
[26] The polymer electrolyte membrane according to any one of [23] to [25], wherein the ion exchange group is a sulfonic acid group.
[27] The polymer electrolyte membrane according to any one of [20] to [26], wherein the ion conductive polymer has one of more repeating units having an ion exchange group selected from the following general formulas (1a) to (4a):
wherein Ar1 to Ar9 each independently represents a divalent aromatic group which has an aromatic ring in the main chain, and also may have a side chain having an aromatic ring, and having an ion exchange group in which at least one of the aromatic ring of the main chain or the aromatic ring of the side chain is bonded directly to the aromatic ring, Z and Z′ each independently represents either CO or SO2, X, X′ and X″ each independently represents either O or S, Y represents a direct bond or a group represented by the following general formula (10), p represents 0, 1 or 2, and q and r each independently represents 1, 2 or 3, and one of more repeating units having substantially no ion exchange group selected from the following general formulas (1b) to (4b):
wherein Ar11 to Ar19 each independently represents a divalent aromatic carbon group which may have a substituent as the side chain, Z and Z′ each independently represents either CO or SO2, X, X′ and X″ each independently represents either O or S, Y represents a direct bond or a group represented by the following general formula (10), p′ represents 0, 1 or 2, and q′ and r′ each independently represents 1, 2 or 3, and
wherein R1 and R2 each independently represents a hydrogen atom, an alkyl group having 1 to 10 carbon atoms which may have a substituent, an alkoxy group having 1 to 10 carbon atoms which may have a substituent, an aryl group having 6 to 18 carbon atoms which may have a substituent, an aryloxy group having 6 to 18 carbon atoms which may have a substituent or an acyl group having 2 to 20 carbon atoms which may have a substituent, and R1 and R2 may be combined to form a ring.
[28] The polymer electrolyte membrane according to any one of [20] to [27], wherein the ion conductive polymer is a copolymer comprising a polymer segment (A) having an ion exchange group and a polymer segment (B) having substantially no ion exchange group.
[29] The polymer electrolyte membrane according to any one of [20] to [28], wherein the ion conductive polymer is a block copolymer comprising a block (A) having an ion exchange group and a block (B) having substantially no ion exchange group.
[30] The polymer electrolyte membrane according to any one of [20] to [29], which has a structure microphase-separated into at least two or more phases.
[31] The polymer electrolyte membrane according to any one of [20] to [30], which contains, as the ion conductive polymer, a block copolymer comprising a block (A) having an ion exchange group and a block (B) having substantially no ion exchange group, and also has a microphase-separated structure containing a phase having a high density of a block (A) having an ion exchange group and a phase having a high density of a block (B) having substantially no ion exchange group.
[32] The polymer electrolyte membrane according to any one of claims 20 to 31, wherein the ion conductive polymer has at least one block (A) having an ion exchange group and at least one block (B) having substantially no ion exchange group, the block (A) having an ion exchange group has a repeating unit represented by the following general formula (4a′):
wherein m represents an integer of 5 or more, Ar9 represents a divalent aromatic group, in which the divalent aromatic group may be substituted with a fluorine atom, an alkyl group having 1 to 10 carbon atoms which may have a substituent, an alkoxy group having 1 to 10 carbon atoms which may have a substituent, an aryl group having 6 to 18 carbon atoms which may have a substituent, an aryloxy group having 6 to 18 carbon atoms which may have a substituent, or an acyl group having 2 to 20 carbon atoms which may have a substituent, and Ar9 has an ion exchange group bonded directly to an aromatic ring constituting the main chain bonded indirectly via the side chain, and the block (B) having substantially no ion exchange group has one or more repeating structures selected from the following general formulas (1b′), (2b′) and (3b′):
wherein n represents an integer of 5 or more, Ar11 to Ar18 each independently represents a divalent aromatic group, in which the divalent aromatic group may be substituted with an alkyl group having 1 to 18 carbon atoms, an alkoxy group having 1 to 10 carbon atoms, an aryl group having 6 to 10 carbon atoms, an aryloxy group having 6 to 18 carbon atoms or an acyl group having 2 to 20 carbon atoms, and other symbols are the same as those in the general formulas (1b) to (3b).
[33] The polymer electrolyte membrane according to any one of [20] to [32], wherein the ion conductive polymer has at least one block (A) having an ion exchange group and at least one block (B) having substantially no ion exchange group, and the ion exchange group is bonded directly to the aromatic ring of the main chain in the block (A) having an ion exchange group.
[34] The polymer electrolyte membrane according to any one of [20] to [33], wherein the ion conductive polymer has at least one block (A) having an ion exchange group and at least one block (B) having substantially no ion exchange group, and both the block (A) having an ion exchange group and the block (B) having substantially no ion exchange group have substantially no substituent containing a halogen atom.
[35] A laminate, wherein the ion conductive polymer electrolyte membrane according to any one of [20] to [34] is laminated on a supporting substrate.
[36] The laminate according to [35], wherein the surface bonded to the polymer electrolyte membrane of the supporting substrate is formed of a metal or a metal oxide.
[37] The laminate according to [35] or [36], wherein the supporting substrate is a continuous supporting substrate which is a film containing a metal or a metal oxide on the surface.
According to the present invention, it is possible to obtain a polymer electrolyte membrane whose both surfaces have almost the same surface properties by applying a polymer electrolyte solution on the surface of a supporting substrate through flow casting when a polymer electrolyte membrane is produced by a so-called solution casting method. Therefore, in continuous production of the polymer electrolyte membrane, a different treatment may not be performed considering properties of front and back surfaces of the polymer electrolyte membrane. Therefore, it is possible to provide a polymer electrolyte membrane having extremely excellent handling properties from the viewpoint of industrial production. When a membrane-electrode assembly is produced by attaching an electrode to the polymer electrolyte membrane, the resulting membrane-electrode assembly has good bondability between a membrane and an electrode without performing complicated post-processing such as a surface treatment after membrane formation. Therefore, the resulting membrane is industrially useful polymer electrolyte membrane for a high-functional solid polymer type fuel cell.
The polymer electrolyte membrane of the present invention will now be described in detail. The polymer electrolyte is an electrolyte resin containing at least one ion conductive polymer and a membrane made of the polymer electrolyte is referred to as a polymer electrolyte membrane. The polymer electrolyte membrane preferably contains the ion conductive polymer in an amount of 50% by weight or more, preferably 70% by weight or more, and particularly preferably 90% by weight or more.
The ion conductive polymer means a polymer which substantially has an ion exchange group, and has a group associated with ionic conduction, especially proton conduction, when used as an electrolyte membrane for a solid polymer type fuel cell.
In the polymer electrolyte membrane of the present invention, an amount of the ion exchange group which is responsible for ion conductivity to be introduced is preferably from 0.5 meq/g to 4.0 meq/g, and more preferably from 1.0 meq/g to 2.8 meq/g, in terms of ion exchange capacity. The ion exchange capacity, which indicates the amount of an ion exchange group to be introduced, is preferably 0.5 meq/g or more, since proton conductivity further increases and thus more excellent function required as a polymer electrolyte for a fuel cell is attained. In contrast, the ion exchange capacity, which indicates the amount of an ion exchange group to be introduced, is preferably 4.0 meq/g or less, since water resistance is more improved.
The polymer electrolyte membrane of the present invention is characterized in that it is a polymer electrolyte membrane containing at least one ion conductive polymer in which at least any one surface of the polymer electrolyte membrane is not subjected to the surface treatment, and also a difference in a contact angle against water between one surface and the other surface of the polymer electrolyte membrane is 30° or less. The difference in a contact angle against water between both surfaces is preferably 20° or less, and more preferably 10° or less.
When the difference in a contact angle against water between both surfaces is within 30° or less, the polymer electrolyte membrane can be easily processed without taking account of surface properties of front and back surfaces of the polymer electrolyte membrane, and thus the polymer electrolyte membrane having extremely is excellent in handling properties. For example, in the production of a membrane-electrode assembly for a solid polymer type fuel cell, the membrane-electrode assembly can be easily produced by subjecting a similar surface treatment to front and back surfaces of the polymer electrolyte membrane. As described above, in a treatment of processing the polymer electrolyte membrane, surface properties of front and back surfaces of the membrane are preferably identical and the difference in a contact angle against water between both surfaces of the membrane is preferably smaller.
The contact angle against water of any of one surface and the other surface of the membrane is preferably 10° or more and 60° or less, and more preferably 20° or more and 50° or less.
The contact angle against water of both surface is preferably 10° or more since the surface of the polymer electrolyte membrane is more excellent in dimensional stability upon water absorption.
The contact angle against water of both surfaces is preferably 60° or less since bondability between the produced polymer electrolyte membrane and the electrode for a fuel cell more increases.
The contact angle against water of one surface and the other surface of the polymer electrolyte membrane is a value of the polymer electrolyte membrane which is not subjected to post-processing such as a surface treatment to the polymer electrolyte membrane.
The membrane, which is not subjected to a post-processing treatment such as surface treatment, is industrially very useful since the number of the step of the membrane formation step can be decreased. Since the membrane surface may cause chemical or physical degradation when subjected to a surface treatment, it is preferred that the membrane is not subjected to a surface treatment.
According to the present invention, it is possible to impart a difference in a contact angle of 30° or less between both surfaces of the polymer electrolyte membrane by applying a polymer electrolyte solution on the surface of a proper supporting substrate through flow casting without performing post-processing such as a surface treatment after membrane formation when the polymer electrolyte membrane is formed by a so-called solution casting method. Namely, it is possible to impart a sufficiently small difference in hydrophilicity between both surfaces of the membrane without subjecting both surfaces to a special surface treatment after membrane formation using a solution casting method.
The fact that post-processing such as surface treatment is not performed means that the surface state of the membrane obtained by the membrane formation step including flow casting does not undergo an additional change after the flow casting step.
Examples of the surface treatment include hydrophilicizing treatments such as corona treatment and plasma treatment, and water repelling treatments such as fluorination treatment. After subjecting to the hydrophilicizing treatment, a hydrophilic group is usually imparted on the surface, or the surface is a rough surface having fine unevenness. After subjecting to the water repelling treatment, a water-repellant group is usually imparted to the surface.
Therefore, specific examples of a state of the polymer electrolyte membrane which is not subjected to the surface treatment include a state in which a functional group other than an original functional group peculiar to the polymer electrolyte membrane is not imparted to the surface, or the imparted functional group is an original functional group peculiar to the polymer electrolyte membrane but an existing amount thereof does not vary (the amount of the functional group does not increase or decrease), or the surface is not intentionally roughened after the membrane formation step. As described above, the surface treatment means a treatment which causes an irreversible change to the polymer electrolyte membrane. Therefore, in the polymer electrolyte constituting the polymer electrolyte membrane, the ion exchange reaction is not included in a category of the surface treatment since the ion exchange reaction itself is a reversible reaction.
As the method for producing a polymer electrolyte membrane of the present invention, a method for forming a membrane from a solution state (so-called solution casting method) is used particularly preferably.
Specifically, the polymer electrolyte membrane is preferably formed by dissolving at least one kind of an ion conductive polymer and, if necessary, other components such as polymers other than the ion conductive polymer, and additives in a proper solvent, applying the polymer electrolyte solution on a specific substrate through flow casting (cast membrane formation) and removing the solvent.
The polymer electrolyte solution may be prepared by separately adding two or more kinds of ion conductive polymers to a solvent, or separately adding the ion conductive polymer and other components to a solvent, for example, the polymer electrolyte solution may be prepared by separately adding and dissolving two or more components constituting a polymer electrolyte in a solvent.
The solvent to be used in membrane formation is not specifically limited as long as it can dissolve the ion conductive polymer and optionally added other components and can be removed after the addition. Examples of preferably used solvent include aprotic polar solvents such as dimethylformamide (DMF), dimethylacetamide (DMAc), N-methyl-2-pyrrolidone (NMP) and dimethyl sulfoxide (DMSO); chlorine-based solvents such as dichloromethane, chloroform, 1,2-dichloroethane, chlorobenzene and dichlorobenzene; alcohols such as methanol, ethanol and propanol; and alkylene glycol monoalkyl ethers such as ethylene glycol monomethyl ether, ethylene glycol monoethyl ether, propylene glycol monomethyl ether and propylene glycol monoethyl ether. These solvents can be used alone, or two or more kinds of solvents can be optionally used in combination. Among these solvents, DMSO, DMF, DMAc and NMP are preferable because of high solubility of the polymer.
With respect to the polymer electrolyte membrane produced by the present invention, chemical stabilizers can be added to the polymer electrolyte so as to enhance chemical stability such as oxidation resistance or radical resistance as long as the effects of the present invention are not adversely affected. Examples of the stabilizers to be added include antioxidants described in JP-A No. 2003-201403, JP-A No. 2003-238678 and JP-A No. 2003-282096. Alternatively, it is possible to contain, as the chemical stabilizer, phosphonic acid group-containing polymers represented by the following formulas:
(r=1 to 2.5, s=0 to 0.5, the number attached to a repeating unit represents a molar fraction of the repeating unit)
(r=1 to 2.5, s=0 to 0.5, the number attached to a repeating unit represents a molar fraction of the repeating unit) described in JP-A No. 2005-38834 and JP-A No. 2006-66391. In the above formulas, “—(P(O)(OH)2)r” and “—(Br)s” represent that the number of phosphonic acid groups is r on average and the number of bromo groups is s on average per biphenylyleneoxy unit.
The content of the chemical stabilizer to be added is preferably within 20% by weight based on the entire polymer electrolyte. When the content is more than the above range, characteristics of the polymer electrolyte membrane may deteriorate.
In the present invention, the supporting substrate to be used in flow casting is preferably a substrate which enables continuous membrane formation. The substrate which enables continuous membrane formation means a substrate which can be retained in the form of a scroll and can endure even under an external force such as bending without causing breakage.
The substrate which enables continuous membrane formation means a substrate which can be take the form of a scroll by winding on a paper or plastic core and it becomes industrially useful since productivity is improved. The substrate preferably has a width of 100 mm or more and a length of 10 m or more, more preferably a width of 150 mm or more and a length of 50 m or more, and still more preferably a width of 200 mm or more and a length of 100 m or more. The substrate also means a substrate which can be continuously unwound or taken up after fixing in the form of a scroll. In general, a substrate such as a glass or metal plate, which has poor flexibility and is broken upon bending, is not preferable.
The substrate to be coated by flow casting is preferably a substrate having heat resistance and dimensional stability which endure drying conditions upon cast membrane formation, and a substrate having solvent resistance and water resistance to the above-described solvent is preferable. It is preferred that the polymer electrolyte membrane does not firmly adhere to the substrate and can be peeled after application and drying. As used herein, “having heat resistance and dimensional stability” means that heat deformation does not occur when drying is conducted using a drying oven so as to remove the solvent after flow casting of the polymer electrolyte solution. As used herein, “having solvent resistance” means that the substrate itself is not substantially dissolved in the solvent in the polymer electrolyte solution. As used herein, “having water resistance” means that the substrate itself is not substantially dissolve in an aqueous solution having pH of 4.0 to 7.0. Furthermore, “having solvent resistance” and “having water resistance” mean concept in which chemical degradation is not caused by the solvent or water, and also the substrate occurs neither swelling nor shrinkage and has excellent dimensional stability.
Control of the contact angle against the film surface will be described. Wettability of the surface of the film depends on a combination of the polymer electrolyte and the substrate, and is represented by a difference in a contact angle. The polymer electrolyte is preferably a copolymer when compared with a homopolymer, and a block copolymer is more preferably among the copolymer. Among the block copolymer, a block copolymer having a microphase-separated structure is particularly preferable for the following reason. Since the microphase-separated structure has a microscopic aggregate, the contact angle is controlled by a strong interaction such as affinity or repulsive force between the polymer electrolyte and substrate.
A supporting substrate whose surface to be coated by flow casting is formed of a metal or metal oxide is suited as a supporting substrate in which a contact angle against water of both surfaces of the polymer electrolyte membrane can be easily decreased by application through flow casting.
Examples of the material of the substrate surface to be coated by flow casting include a substrate made of a metal or metal oxide layer. Specific examples of the material of the metal layer include aluminum, copper, iron, stainless steel (SUS), gold, silver, platinum, or alloys thereof. Examples of the material of metal oxide layer include oxide and silicon oxide of the above metals.
The metals or metal oxides may support alone, or may be formed on a film layer made of a resin using deposition or sputtering. Examples of the resin film include an olefin-based film, a polyester-based film, a polyamide-based film, a polyimide-based film and a fluorine-based film. Among these films, a polyester-based film and a polyimide-based film are preferable since they are excellent in heat resistance, dimensional stability and solvent resistance. Examples of the material of the polyester-based film include polyethylene terephthalate, polyethylene naphthalate, polybutylene terephthalate and aromatic polyester. Among these materials, polyethylene terephthalate is industrially preferable also in view of versatility and cost, not only from the above described various characteristics.
Among combinations of a resin film layer and a metal thin film or metal oxide thin film layer, preferred is a combination in which the resin film layer is made of polyethylene terephthalate and the metal thin film layer or metal oxide thin film layer is an aluminum laminate layer, an aluminum-deposited layer, an alumina-deposited layer, a silica-deposited layer or an alumina-silica dual-deposited layer. These laminate film includes a laminate film which is commonly used in packaging materials.
The alumina-deposited polyethylene terephthalate film includes, for example, an alumina-deposited film VARIALOX (trade name) manufactured by TORAY ADVANCED FILM Co., Ltd. The silica-deposited polyethylene terephthalate film includes MOS (trade name) manufactured by Oike & Co., Ltd. The alumina-silica dual-deposited polyethylene terephthalate film includes ECOSYAL (trade name) manufactured by Toyobo Co., Ltd.
The film containing a metal or metal oxide on the surface can take the form of a continuous long flexible substrate and can be retained and used as a scroll, and is preferably used when a polymer electrolyte membrane is continuously formed.
According to the purposes, the substrate may be subjected to a surface treatment which can change wettability of the surface of the supporting substrate. Examples of the treatment capable of changing wettability of the surface of the supporting substrate include commonly used methods, for example, hydrophilicizing treatments such as corona treatment and plasma treatment, and water repelling treatments such as fluorination treatment.
A laminate comprising a supporting substrate and a polymer electrolyte membrane laminated on the supporting substrate is obtained through the above membrane formation step. This laminate is excellent in the film formation step and handling properties of the resulting polymer electrolyte membrane in the processing step since there is scarcely difference in hydrophilicity between front and back surfaces of the polymer electrolyte membrane constituting the laminate and both surfaces of the polymer electrolyte membrane can be handled in the same way.
The laminate may be stored and circulated as it is. When the supporting substrate is a flexible substrate, the laminate can be treated in a scroll-like form.
A polymer electrolyte membrane is obtained by removing a supporting substrate from the laminate. The supporting substrate may be usually removed by peeling from the laminate.
The thickness of the polymer electrolyte membrane in the present invention is not specifically limited, and is preferably from 10 to 300 μm. A membrane having a thickness of 10 μm or more is preferable since it is excellent in practical strength, while a membrane having a thickness of 300 μm or less is preferable since membrane resistance decreases and thus characteristics of an electrochemical device tend to be more improved. The thickness of the membrane can be controlled by a concentration of a solution and a coating thickness on a base material.
The polymer electrolyte membrane obtained by the present invention is characterized in that a difference in a contact angle against water between one surface and the other surface of the membrane is less than 30° even when post-processing such as a surface treatment is not conducted after membrane formation.
Since this polymer electrolyte membrane has no difference between front and back surfaces and both surfaces of the polymer electrolyte membrane can be handled in the same way, the polymer electrolyte membrane is excellent in handling properties in the membrane formation step, and thus the polymer electrolyte membrane is industrially advantageous.
It is preferred that the ion conductive polymer in the present invention has an aromatic ring in the main chain, and also has an ion exchange group bonded directly to the aromatic ring or bonded indirectly to the aromatic ring via an atom or atomic group.
The ion conductive polymer in the present invention may have a side chain.
The ion conductive polymer in the present invention has an aromatic ring in the main chain, and also may have a side chain having an aromatic ring, and preferably has an ion exchange in which at least one of the aromatic ring of the main chain and the aromatic ring of the side chain is bonded directly to the aromatic ring.
The ion exchange group is preferably a cation exchange group.
The polymer electrolyte membrane of the present invention is preferably a hydrocarbon-based polymer electrolyte membrane, namely a membrane formed of a polymer electrolyte containing a hydrocarbon-based ion conductive polymer.
The hydrocarbon-based polymer electrolyte preferably contains the hydrocarbon-based ion conductive polymer in the amount of 50% by weight or more, more preferably 70% by weight or more, and particularly preferably 90% by weight or more. As long as the effects of the present invention are not adversely affected, other polymers, non-hydrocarbon-based ion conductive polymers and additives may be contained.
The hydrocarbon-based ion conductive polymer typically does not contain any fluorine, or may partially substituted with fluorine. Examples of the hydrocarbon-based ion conductive polymer include engineering resins having an aromatic main chain, such as polyether ether ketone, polyether ketone, polyethersulfone, polyphenylene sulfide, polyphenylene ether, polyether ethersulfone, polyparaphenylene and polyimide; general-purpose resins such as polyethylene and polystyrene; and polymers obtained by introducing an ion exchange group in a copolymer having a combination of plural kinds of repeating unit constituting resins. Since the main chain preferably has an aromatic ring, polymers obtained by introducing an ion exchange group in a resin having a combination of plural kinds of repeating unit constituting the engineering resin or the engineering resin are preferably since a polymer electrolyte membrane having more excellent heat resistance is obtained.
The ion exchange group is preferably a cation exchange group such as a sulfonic acid group (—SO3H), a carboxylic acid group (—COOH), a phosphoric acid group (—OP(O)(OH)2), a phosphonic acid group (—P(O)(OH)2) or a sulfonylimide group (—SO2—NH—SO2—). Among these groups, a sulfonic acid group is preferable.
The hydrocarbon-based polymer electrolyte has an advantage that it is cheap when compared with the fluorine-based polymer electrolyte.
The polymer electrolyte used in the present invention is preferably a copolymer composed of a repeating unit having an ion exchange group and a repeating unit having no ion exchange group since it is easy to control a contact angle against water as described above. The type of copolymerization of the copolymer may be any of random copolymerization, block copolymerization, graft copolymerization and alternating copolymerization, or a combination of these types of copolymerization. In view of ease of controlling a contact angle, a block copolymer and a graft copolymer each having at least one polymer segment (A) having an ion exchange group and at least one polymer segment (B) having substantially no ion exchange group are more preferable. A block copolymer is more preferable.
In the present invention, the segment or block has an “ion exchange group” means a segment or block having 0.5 or more ion exchange group on average per one repeating unit, and more preferably 1.0 or more ion exchange groups on average per one repeating unit.
On the other hand, the segment or block “has substantially no ion exchange group” means a segment or block having less than 0.5 ion exchange group on average per one repeating unit, more preferably less than 0.1 ion exchange group on average per one repeating unit, and still more preferably less than 0.05 ion exchange group on average per one repeating unit.
When the polymer electrolyte used in the present invention contains a block copolymer, the block copolymer preferably has at least one block (A) having an ion exchange group and at least one block (B) having substantially no ion exchange group.
When the polymer electrolyte used in the present invention contains a block copolymer, the polymer electrolyte membrane preferably forms a microphase-separated structure. The microphase-separated structure as used herein means a structure obtained as a result of the occurrence of microscopic phase separation of an order of a molecular chain size by bonding different kinds of polymer segments through a chemical bond in a block copolymer or a graft copolymer. That is, it means a structure in which a microphase (microdomain) with a high density of a block (A) having an ion exchange group and a microphase (microdomain) with a high density of a block (B) having substantially no ion exchange group coexist and each microdomain structure has a domain width, namely an identity period of several nanometers to several hundreds of nanometers when observed using a transmission electron microscope (TEM). A polymer electrolyte membrane having a microdomain structure of 5 nm to 100 nm is preferable.
Examples of the ion conductive polymer to be used in the polymer electrolyte of the present invention include those having a structure in conformity with JP-A No. 2005-126684 and JP-A No. 2005-139432.
Specific examples of the ion conductive polymer of the present invention is preferably containing, as repeating units, any one or more repeating units of the general formulas (1a), (2a), (3a), (4a) and any one or more repeating units of the general formulas (1b), (2b), (3b) and (4b). Examples of the type of polymerization include block copolymerization, alternating copolymerization and random copolymerization.
In the present invention, a block copolymer is preferably a copolymer comprising one or more blocks composed of repeating units having an ion exchange group selected from the general formulas (1a), (2a), (3a) and (4a) and one or more blocks composed of repeating units having substantially no ion exchange group selected from the general formulas (1b), (2b), (3b) and (4b), and more, preferably a copolymer comprising the following blocks:
<i> block composed of a repeating unit (1a), and a block of a repeating unit (1b),
<ii> block composed of a repeating unit (1a), and a block composed of a repeating unit (2b),
<iii> block composed of a repeating unit (2a), and a block composed of a repeating unit (1b),
<iv> block composed of a repeating unit (2a), and a block composed of a repeating unit (2b),
<v> block composed of a repeating unit (3a), and a block composed of a repeating unit (1b),
<vi> block composed of a repeating unit (3a), and a block composed of a repeating unit (2b),
<vii> block composed of a repeating unit (4a), and a block composed of a repeating unit (1b), and
<viii> block composed of a repeating unit (4a), and a block composed of a repeating unit (2b).
The block copolymer is more preferably a copolymer having the above-described <ii>, <iii>, <iv>, <vii> and <viii>, and particularly preferably a copolymer comprising the above-described <vii> and <viii>.
In more preferable block copolymer of the present invention, the repeating number of (4a), namely m in the above general formula (4a′) represents an integer of 5 or more, and is preferably within a range from 5 to 1,000, and more preferably from 10 to 500. m is preferably 5 or more since the resulting polymer electrolyte for a fuel cell has sufficient proton conductivity. m is preferably 1,000 or less since it is easy to produce.
Ar9 in the formula (4a′) represents a divalent aromatic group. Examples of the divalent aromatic group include divalent monocyclic aromatic groups such as 1,3-phenylene and 1,4-phenylene groups; divalent condensed-ring aromatic groups such as 1,3-naphthalenediyl, 1,4-naphthalenediyl, 1,5-naphthalenediyl, 1,6-naphthalenediyl, 1,7-naphthalenediyl, 2,6-naphthalenediyl and 2,7-naphthalenediyl groups; and heteroaromatic groups such as pyridinediyl, quinoxalinediyl and thiophenediyl groups. Among these groups, divalent monocyclic aromatic groups are preferable.
Ar9 may be substituted with an alkyl group having 1 to 10 carbon atoms which may have a substituent, an alkoxy group having 1 to 10 carbon atoms which may have a substituent, an aryl group having 6 to 18 carbon atoms which may have a substituent, an aryloxy group having 6 to 18 carbon atoms which may have a substituent, or an acyl group having 2 to 20 carbon atoms which may have a substituent.
Ar9 has at least one ion exchange group on an aromatic ring constituting the main chain. The ion exchange group is preferably an acidic group (a cation exchange group), and more preferably a sulfonic acid group, a phosphonic acid group and a carboxylic acid group. Among these groups, a sulfonic acid group is preferable. These ion exchange groups may be partially or entirely replaced by a metal ion to form a salt. When used as a polymer electrolyte membrane for a fuel cell, it is preferred that the entire ion exchange groups are substantially in a state of a free acid.
Preferred examples of the repeating structure represented by the formula (4a′) include the following formula.
In a more preferred block copolymer of the present invention, the number of repeating units (1b) to (3b), namely n in the above general formulas (1b′) to (3b′) represents an integer of 5 or more, and is preferably within a range from 5 to 1,000, and more preferably from 10 to 500. n is preferably 5 or more since the resulting polymer electrolyte for a fuel cell has sufficient proton conductivity. n is preferably 1,000 or less since it is easy to produce.
Ar11 to Ar18 in the formulas (1b′) to (3b′) each independently represents a divalent aromatic group. Examples of the divalent aromatic group include divalent monocyclic aromatic groups such as 1,3-phenylene and 1,4-phenylene groups; divalent condensed-ring aromatic groups such as 1,3-naphthalenediyl, 1,4-naphthalenediyl, 1,5-naphthalenediyl, 1,6-naphthalenediyl, 1,7-naphthalenediyl, 2,6-naphthalenediyl and 2,7-naphthalenediyl groups; and heteroaromatic groups such as pyridinediyl, quinoxalinediyl and thiophenediyl groups. Among these groups, divalent monocyclic aromatic groups are preferable.
Ar11 to Ar18 may be substituted with an alkyl group having 1 to 18 carbon atoms, an alkoxy group having 1 to 10 carbon atoms, an aryl group having 6 to 10 carbon atoms, an aryloxy group having 6 to 18 carbon atoms, or an acyl group having 2 to 20 carbon atoms.
Specific examples of the ion conductive polymer include the following structures.
In the above-described (1) to (26), “block” means a block copolymer comprising each block of a repeating unit in parenthesis. These blocks may be in the form of being directly bonded, or may be in the form of being linked via a proper atom or atomic group.
Ion conductive polymers are more preferably the above-described (2), (7), (8), (16), (18) and (22) to (25), and particularly preferably (16), (18), (22), (23) and (25).
When the ion conductive polymer is the above block copolymer, it is particularly preferred that both a block (A) having an ion exchange group and a block (B) having substantially no ion exchange group have substantially no substituent containing a halogen atom. Examples of the halogen atom include fluorine, chlorine, bromine and iodine atoms.
As used herein, “have substantially no substituent containing a halogen atom” means that the blocks have not 0.05 or more halogen atoms per repeating unit of the ion conductive polymer.
Examples of the substituent, which may be contained, include an alkyl group, an alkoxy group, an aryl group, an aryloxy group and an acyl group, and an alkyl group is preferable. These substituents preferably have 1 to 20 carbon atoms and include, for example, substituents having less carbon atoms such as a methyl group, an ethyl group, a methoxy group, an ethoxy group, a phenyl group, a naphthyl group, a phenoxy group, a naphthyloxy group, an acetyl group and a propionyl group.
It is not preferred that the block copolymer contains a halogen atom since hydrogen fluoride, hydrogen chloride, hydrogen bromide or hydrogen iodide may be generated during operation of a fuel cell, thus causing corrosion of a fuel cell member.
The molecular weight of the proton conductive polymer is preferably from 5,000 to 1,000,000, and particularly preferably from 15,000 to 400,000, in terms of a polystyrene equivalent number average molecular weight.
It is expected that the polymer electrolyte membrane obtained by the present invention is used in various fields.
For example, the polymer electrolyte of the present invention can be used as a diaphragm for an electrochemical device such as fuel cell. This polymer electrolyte membrane is excellent in characteristics required as an electrolyte membrane for a fuel cell and has high utility value since both surfaces of the membrane have good affinity with an electrode for a fuel cell.
When used as an electrolyte membrane for a fuel cell, since there is scarcely a difference in hydrophilicity between both surfaces of the membrane and the membrane can be used regardless of front and back surfaces, and thus it is industrially advantageous. Because of high affinity between the membrane and the electrode in the post-step of attaching the electrode, the effects of enhancing bondability at the interface between the membrane and the electrode can be expected.
Therefore, the polymer electrolyte membrane produced by the method of the present invention is an industrially useful polymer electrolyte membrane used for a high-functional type solid polymer type fuel cell.
A fuel cell using the membrane of the present invention will now be described.
The fuel cell of the present invention can be produced by bonding a catalyst and a conductive material as a current collector on both surfaces of a proton conductive polymer electrolyte membrane.
As used herein, the catalyst is not specifically limited as long as it can activate an oxidation-reduction reaction with hydrogen or oxygen, and known catalysts can be used. It is preferred to use fine particles of platinum or a platinum-based alloy. Fine particles of platinum or a platinum-based alloy are often used in a state of being supported on a granular or fibrous carbon such as active carbon or graphite.
A catalyst layer can be obtained by applying and drying a paste, which is obtained by mixing platinum supported on carbon with an alcohol solution of a perfluoroalkylsulfonic acid resin as a polymer electrolyte, on a gas diffusion layer and/or a polymer electrolyte membrane and/or a polymer electrolyte composite membrane. As a specific method, for example, a known method such as a method described in J. Electrochem. Soc.: Electrochemical Science and Technology, 1988, 135 (9), 2209 can be used.
In place of the perfluoroalkylsulfonic acid resin as the polymer electrolyte, the proton conductive polymer electrolyte of the present invention can be used as a catalyst composition.
As the conductive material as the current collector, known materials can be used, and a porous carbon woven fabric, carbon nonwoven fabric or carbon paper is preferable since it efficiently transfers a raw gas to the catalyst.
The fuel cell thus obtained of the present invention can be used as various fuel cells using a hydrogen gas, a reformed hydrogen gas or methanol as a fuel.
While embodiments of the present invention has been described above, the embodiments of the present invention disclosed in the above description are simply exemplifications, and it is not intended to limit the scope of the invention to the particular form set forth. It is intended to cover such alternatives, modifications, and equivalents as may be included within the spirit and scope of the present invention as defined by the appended claims.
The present invention will be described by way of Examples, but the present invention is not limited to the following Examples. Methods for the measurement of physical properties of the present invention are described below.
Using a halogen moisture meter set at a heating temperature of 105° C., a dry weight of a polymer electrolyte membrane to be measured was determined. The polymer electrolyte membrane was immersed in 5 mL of an aqueous 0.1 mol/L sodium hydroxide solution, further mixed with 50 mL of ion exchanged water and then allowed to stand for 2 hours. Titration was conducted by gradually adding 0.1 mol/L hydrochloric acid to the solution in which the polymer electrolyte membrane was immersed thereby determining a neutral point. From the dry weight of the polymer electrolyte membrane and the amount of hydrochloric acid required for neutralization, an ion exchange capacity (unit: meq/g) of the polymer electrolyte membrane was calculated.
A polystyrene equivalent number average molecular weight (Mn) and a weight average molecular weight (Mw) were measured by gel permeation chromatography (GPC) under the following conditions. In the measurement, any one of the following mobile phase was used as a mobile phase (eluant).
[Mobile phase 1] DMAc (LiBr was added in a concentration of 10 mmol/dm3)
[Mobile phase 2] DMF (LiBr was added in a concentration of 10 mmol/dm3)
Each of polymer electrolyte membranes of Examples and Comparative Examples was allowed to stand under an atmosphere at 23° C. and 50% RH for 24 hours in a state of being peeled from a supporting substrate. Using a contact angle meter (Model CA-A, manufactured by Kyowa Interface Science Co., Ltd.), a contact angle against water droplets of a membrane surface was determined by a drop method. Water droplets having a diameter of 2.0 mm were dropped on a polymer electrolyte membrane and then the contact angle after 5 seconds after the dropping was used as a measured value.
Each of polymer electrolyte membranes of the Examples and Comparative Examples was immersed in an aqueous stain solution (concentration of potassium iodide: 15%, concentration of iodine: 5%) at room temperature for 30 minutes and then embedded in a precured epoxy resin. Furthermore, a 60 nm-thick piece was cut out under dry conditions at room temperature using a microtome. The cut out piece was collected on a Cu mesh and then observed at an acceleration voltage of 300 kV using a transmission electron microscope (manufactured by Hitachi, Ltd. H9000NAR).
To 6 mL of a commercially available 5% by weight Nafion solution (solvent: mixture of water and lower alcohol), 0.83 g of a platinum (50% by weight of platinum)-supported carbon (SA50BK, manufactured by N.E. CHEMCAT CORPORATION) was added and then 9 mL of ethanol was added. The resulting mixture was ultrasonicated for 1 hour and stirred with a stirrer for 5 hours to obtain a catalyst ink.
The catalyst ink was applied on a Teflon (registered trademark) sheet using a doctor blade and then the solvent was removed in an oven at 80° C. for 1 hour to obtain a transfer sheet.
Each of polymer electrolyte membranes of Examples and Comparative Examples was cut out into pieces measuring 5 cm in length and 5 mm in width and then immersed in water. After taking out the cut out polymer electrolyte membrane, the electrolyte membrane and a transfer sheet were laminated upon another, interposed between two SUS plates and then hot pressed (press conditions: 100 kgf/cm2, 100° C., 10 minutes). The case where an electrode is uniformly transferred in the electrolyte membrane was rated “good”, whereas, the case where an electrode is partially peeled or not uniformly transferred was rated “poor”.
Under an argon atmosphere, in a flask equipped with an azeotropic distillation device, 142.2 parts by weight of DMSO, 55.6 parts by weight of toluene, 5.7 parts by weight of sodium 2,5-dichlorobenzenesulfonate, 2.1 parts by weight of the following chloro-terminated polyethersulfone:
(manufactured by Sumitomo Chemical Co., Ltd., Sumicaexcel PES5200P) and 9.3 parts by weight of 2,2′-bipyridyl were charged, followed by stirring. After raising a bath temperature to 100° C., moisture in the system was azeotropically dehydrated by distilling off toluene with heating under reduced pressure. After cooling to 65° C., the pressure was returned to normal pressure. To this was added 15.4 parts by weight of bis(1,5-cyclooctadiene)nickel(0), followed by heating to 70° C. and further stirring at the same temperature for 5 hours. After air cooling, the reaction solution was poured into a large amount of methanol thereby precipitating a polymer and the polymer was separated by filtration. After repeating the operation of washing with 6 mol/L hydrochloric acid and filtration several times, the filtrate was washed until it is neutralized, and then dried under reduced pressure to obtain 3.0 parts by weight (IEC=2.2 meq/g, Mn=103,000, Mw=257,000 [mobile phase 2]) of the objective polyarylene-based block copolymer.
Cast membrane formation was carried out using a continuous drying furnace. Using membrane thickness variable doctor blade, a polymer electrolyte solution was adjusted to a desired membrane thickness and continuously applied on a supporting substrate by flow casting, and then almost all of a solvent was removed by continuously transferring into a drying furnace. Drying conditions are described below.
Drying conditions: Temperature; 80° C., Time; 66 minutes (The temperature means a preset temperature of a drying furnace and the time means the time during which the membrane formed polymer electrolyte membrane enters into the drying furnace and comes out of the surface.)
After drying, the polymer electrolyte membrane was washed with ion exchanged water to completely remove the solvent. The membrane was immersed in 2 N hydrochloric acid for 2 hours, washed again with ion exchanged water and then air-dried to obtain a polymer electrolyte membrane.
The polyarylene-based block copolymer (IEC=2.2 meq/g, Mn=103,000, Mw=257,000 [mobile phase 2], IEC is an ion exchange capacity, Mn is a polystyrene equivalent number average molecular weight, Mw is a polystyrene equivalent weight average molecular weight, the same shall apply hereinafter) obtained in Synthesis Example 1 is referred to as BCP-1. BCP-1 was dissolved in DMSO to prepare a solution having a concentration of 10% by weight was prepared. Using the resulting solution and a silica-deposited PET measuring 300 mm in width and 1,000 m in length (manufactured by Oike & Co., Ltd., membrane thickness 12 μm) as a supporting substrate, a polymer electrolyte membrane having a membrane thickness of about 30 μm was produced by a method of the membrane formation condition 1. As a result of TEM observation, it was found that the polymer electrolyte membrane has a microphase-separated structure, and both a hydrophilic phase and a hydrophobic phase form a continuous phase.
A mixture (weight ratio of 90:10) of the polyarylene-based block copolymer (BCP-1) obtained in Synthesis Example 1 and a phosphonic acid group-containing polymer (referred to as AD-1) synthesized with reference to the method described in Reference Example 3 (see the following formula) of JP-A No. 2005-38834 was dissolved in DMSO to prepare a solution having a concentration of 10% by weight. Using the resulting solution and an aluminum sheet (membrane thickness 200 μm) measuring 300 mm in width and 1,000 m in length as a supporting substrate, a polymer electrolyte membrane having a membrane thickness of about 30 μm was produced by a method of membrane formation example 1. As a result of TEM observation, it was found that the polymer electrolyte membrane has a microphase-separated structure, and both a hydrophilic phase and a hydrophobic phase form a continuous phase.
(r=1.9, s=0.0, the number attached to a repeating unit represents a molar fraction of the repeating unit)
A mixture (weight ratio of 90:10) of a block copolymer (IEC=2.2 meq/g, Mn=116,000, Mw=228,000 [mobile phase 2]: BCP-2) of a synthesis lot different from that of BCP-1 synthesized according to the polymerization method of Synthesis Example 1 and a phosphonic acid group-containing polymer (referred to as AD-2) synthesized with reference to the method described in JP-A No. 2006-66391 ([0059], see the following formula) was dissolved in DMSO to prepare a solution having a concentration of 10% by weight. Using the resulting solution and alumina-deposited PET measuring 300 mm in width and 1,000 m in length (membrane thickness 100 μm) as a supporting substrate, a polymer electrolyte membrane having a membrane thickness of about 30 μm was produced by a method of membrane formation condition 1. As a result of TEM observation, it was found that the polymer electrolyte membrane has a microphase-separated structure, and both a hydrophilic phase and a hydrophobic phase form a continuous phase.
(r=1.6, s=0.0, the number attached to a repeating unit represents a molar fraction of the repeating unit)
A sulfonic acid group-containing block copolymer (IEC=1.8 meq/g, Mn=60,000, Mw=420,000 [mobile phase 1]) synthesized with reference to the method described in JP-A No. 2005-206807 ([0059], see the following formula) (referred to BCP-3) was dissolved in NMP to prepare a solution having a concentration of 13.5% by weight. Using the resulting solution and an alumina-deposited PET measuring 300 mm in width and 1,000 m in length (membrane thickness 100 μm) as a supporting substrate, a polymer electrolyte membrane having a membrane thickness of about 30 μm was produced by a method of membrane formation condition 1. As a result of TEM observation, it was found that the polymer electrolyte membrane has a microphase-separated structure, and both a hydrophilic phase and a hydrophobic phase form a continuous phase.
(the number attached to a repeating unit represents a molar fraction of the repeating unit)
BCP-1 was dissolved in DMSO to prepare a solution having a concentration of 10% by weight. Using the resulting solution and a polyimide film measuring 300 mm in width and 30 m in length (manufactured by DuPont Teijin Co., Ltd. under the trade name of Kapton) as a supporting substrate, a polymer electrolyte membrane having a membrane thickness of about 30 μm was produced by a method of the membrane formation condition 1. As a result of TEM observation, it was found that the polymer electrolyte membrane has a microphase-separated structure, and both a hydrophilic phase and a hydrophobic phase form a continuous phase.
A mixture (weight ratio of 90:10) of BCP-1 and a phosphonic acid group-containing polymer (AD-1) was dissolved in DMSO to prepare a solution having a concentration of 10% by weight. Using the resulting solution and a polyethylene terephthalate (PET) film measuring 300 mm in width and 500 m in length (manufactured by Toyobo Co., Ltd., E5000 grade) as a supporting substrate, a polymer electrolyte membrane having a membrane thickness of about 30 μm was produced by a method of membrane formation example 1. As a result of TEM observation, it was found that the polymer electrolyte membrane has a microphase-separated structure, and both a hydrophilic phase and a hydrophobic phase form a continuous phase.
BCP-3 was dissolved in NMP to prepare a solution having a concentration of 13.5% by weight. Using the resulting solution and a polyethylene terephthalate (PET) film measuring 300 mm in width and 500 m in length (manufactured by Toyobo Co., Ltd., E5000 grade) as a supporting substrate, a polymer electrolyte membrane having a membrane thickness of about 30 μm was produced by a method of membrane formation example 1. As a result of TEM observation, it was found that the polymer electrolyte membrane has a microphase-separated structure, and both a hydrophilic phase and a hydrophobic phase form a continuous phase.
BCP-1 was dissolved in DMSO to prepare a solution having a concentration of 10% by weight. Using the resulting solution and a PET film measuring 300 mm in width and 30 m in length (manufactured by Toyobo Co., Ltd., E5000 grade) as a supporting substrate, a polymer electrolyte membrane having a membrane thickness of about 10 μm was produced by a method of membrane formation example 1. As a result of TEM observation, it was found that the polymer electrolyte membrane has a microphase-separated structure, and both a hydrophilic phase and a hydrophobic phase form a continuous phase.
Polymer electrolyte compositions used in Examples 1 to 4 and Comparative Examples 1 to 4, and kinds of supporting substrates upon membrane formation are shown in Table 1.
A membrane-electrode-bond strength test of Examples 1 to 4 and Comparative Examples 1 to 4 is shown in the table below.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2006-228922 | Aug 2006 | JP | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/JP2007/066819 | 8/23/2007 | WO | 00 | 3/23/2009 |
