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CN101874322B - Composite electrolyte membrane, membrane-electrode assembly, fuel cell, and methods for manufacturing same - Google Patents

Composite electrolyte membrane, membrane-electrode assembly, fuel cell, and methods for manufacturing same Download PDF

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CN101874322B
CN101874322B CN2008801178470A CN200880117847A CN101874322B CN 101874322 B CN101874322 B CN 101874322B CN 2008801178470 A CN2008801178470 A CN 2008801178470A CN 200880117847 A CN200880117847 A CN 200880117847A CN 101874322 B CN101874322 B CN 101874322B
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membrane electrode
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CN101874322A (en
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铃木弘
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Toyota Motor Corp
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    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
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    • Y02E60/50Fuel cells
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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Abstract

A method for manufacturing a composite electrolyte membrane including: a first folding process of folding a laminate (10A) obtained by laminating and integrating an electrolyte sheet (11) having an electrolyte as an electrolyte layer and a reinforcing sheet (12) having a porous polymer material as a reinforcing layer, so that a part of a surface of the laminate (10A) lies on another part of the surface; an impregnation process of impregnating the electrolyte of the folded laminate (10B) into the reinforcing layer; and a hydrolysis process of hydrolyzing the electrolyte impregnated in the laminate (10C).

Description

复合型电解质膜、膜电极组件、燃料电池及用于制造它们的方法Composite electrolyte membrane, membrane electrode assembly, fuel cell and method for manufacturing them

技术领域 technical field

本发明涉及复合型电解质膜、膜电极组件、燃料电池及用于制造它们的方法,更特别地涉及至少具有由电解质构成的电解质层和其中多孔聚合物材料浸渍有所述电解质的加强层的复合型电解质膜、膜电极组件、燃料电池及用于制造它们的方法。The present invention relates to composite electrolyte membranes, membrane electrode assemblies, fuel cells and methods for their manufacture, and more particularly to composite electrolyte membranes having at least an electrolyte layer composed of an electrolyte and a reinforcement layer in which a porous polymer material is impregnated with the electrolyte Type electrolyte membrane, membrane electrode assembly, fuel cell and methods for manufacturing them.

背景技术 Background technique

采用电解质膜的固体聚合物型燃料电池已被研究应用于可移动体,例如汽车,因为这种燃料电池可在低温下工作并具有小的尺寸和重量。特别地,对安装有固体聚合物型燃料电池的燃料电池汽车作为生态环保车的社会关注度在增长。A solid polymer type fuel cell using an electrolyte membrane has been studied for application to a movable body such as an automobile because it operates at a low temperature and has a small size and weight. In particular, social interest in fuel cell vehicles mounted with solid polymer type fuel cells as eco-friendly vehicles is growing.

如图14所示,固体聚合物型燃料电池具有作为主结构元件的膜电极组件(MEA)95。被称为单元电池的单个燃料电池90是通过将膜电极组件夹在具有燃料(氢)气体流路和空气流路的隔板96之间而形成的。膜电极组件95具有这样的结构,其中阳极侧电极(阳极催化剂层)93a层叠在作为离子交换膜的电解质膜91的一侧,而阴极侧电极(阴极催化剂层)93b层叠在另一侧,并且相应的扩散层94a、94b配置在阳极催化剂层93a和阴极催化剂层93b处。As shown in FIG. 14, the solid polymer fuel cell has a membrane electrode assembly (MEA) 95 as a main structural element. A single fuel cell 90 called a unit cell is formed by sandwiching a membrane electrode assembly between separators 96 having fuel (hydrogen) gas flow paths and air flow paths. The membrane electrode assembly 95 has a structure in which an anode side electrode (anode catalyst layer) 93a is laminated on one side of an electrolyte membrane 91 which is an ion exchange membrane, and a cathode side electrode (cathode catalyst layer) 93b is laminated on the other side, and Corresponding diffusion layers 94a, 94b are arranged at the anode catalyst layer 93a and the cathode catalyst layer 93b.

为了确保膜的强度,电解质膜91具有由多孔聚合物材料如聚四氟乙烯(PTFE)构成的加强层,并且该加强层浸渍有电解质。这种具有加强层的复合型电解质膜由图13A所示的流延膜(cast film)形成方法来制造,其在日本专利申请2006-147257号公报(JP-A-2006-147257)中公开。In order to ensure the strength of the membrane, the electrolyte membrane 91 has a reinforcement layer composed of a porous polymer material such as polytetrafluoroethylene (PTFE), and the reinforcement layer is impregnated with an electrolyte. This composite type electrolyte membrane having a reinforcement layer is produced by a cast film forming method shown in FIG. 13A, which is disclosed in Japanese Patent Application Publication No. 2006-147257 (JP-A-2006-147257).

更具体地,首先,将包括电解质聚合物和溶剂的电解质涂覆在正被传送的底衬板片81的一个侧面上,并且使电解质干燥。然后,将由多孔聚合物材料构成的加强板片82配置在干燥了的电解质层的表面上。至少通过在该配置状态下向电解质层和加强板片82施加压力而使电解质从加强板片82的一个表面浸渍到多孔聚合物材料中。然后,将电解质涂覆在加强板片82的另一个表面上并干燥,由此便能制造出复合型电解质膜91,其中至少由多孔聚合物材料构成的加强层和浸渍在加强层中的电解质设置在底衬板片81上。More specifically, first, an electrolyte including an electrolytic polymer and a solvent is coated on one side of the backing sheet 81 being conveyed, and the electrolyte is dried. A reinforcing sheet 82 of porous polymer material is then disposed on the surface of the dried electrolyte layer. Electrolyte is impregnated into the porous polymer material from one surface of the reinforcing sheet 82 at least by applying pressure to the electrolyte layer and the reinforcing sheet 82 in this configured state. Then, the electrolyte is coated on the other surface of the reinforcing sheet 82 and dried, thus a composite electrolyte membrane 91 can be produced, wherein at least the reinforcing layer made of a porous polymer material and the electrolyte impregnated in the reinforcing layer Set on the base sheet 81.

在以上述方式制造的复合型电解质膜91中,如图13B所示,例如,已形成在底衬板片81上的阳极催化剂层93a和阴极催化剂层93b通过利用工具及采用加热和加压来转移,并且催化剂层93a、93b进一步形成在复合型电解质膜91的表面上。In the composite electrolyte membrane 91 produced in the above manner, as shown in FIG. 13B, for example, the anode catalyst layer 93a and the cathode catalyst layer 93b that have been formed on the backing sheet 81 are removed by using tools and applying heat and pressure. transfer, and the catalyst layers 93a, 93b are further formed on the surface of the composite electrolyte membrane 91.

但是,在上述流延膜形成方法中,电解质在不同的工序中浸渍到加强板片的两个表面中。结果,虽然使用的是相同的包含电解质聚合物和溶剂的电解质,但是在复合型电解质膜的两个表面侧之间可能产生膜特性的分散(差异,spread),并且难以获得均一的特性。However, in the cast film forming method described above, the electrolyte is impregnated into both surfaces of the reinforcing sheet in different processes. As a result, although the same electrolyte containing an electrolytic polymer and a solvent is used, dispersion (spread) of membrane characteristics may occur between both surface sides of the composite electrolyte membrane, and it is difficult to obtain uniform characteristics.

此外,由于该制造过程包括在各个表面上涂覆电解质和使溶剂干燥,所以有时难以获得具有高精度的均一膜厚度的电解质膜。此外,与制造设备的精度相对应地,加强板片相对于被涂覆电解质的位置可能从期望的位置偏移。这种偏移特别容易在阳极和阴极催化剂层的配置中发生。In addition, since the manufacturing process includes coating an electrolyte on each surface and drying a solvent, it is sometimes difficult to obtain an electrolyte membrane having a uniform film thickness with high precision. In addition, the position of the reinforcement sheet relative to the electrolyte to be applied may deviate from the desired position corresponding to the precision of the manufacturing equipment. This shift is particularly prone to occur in anode and cathode catalyst layer configurations.

这样,当在电解质膜的两个表面上未获得均一的膜特性时,以及当电解质膜的厚度和催化剂层的位置不在期望的精度范围内时,在电池制造过程中可能导致不良的组装,或者在发电期间可能产生燃料电池性能的分散。In this way, when uniform membrane characteristics are not obtained on both surfaces of the electrolyte membrane, and when the thickness of the electrolyte membrane and the position of the catalyst layer are not within the desired accuracy range, poor assembly may result during battery manufacturing, or Dispersions in fuel cell performance may occur during power generation.

发明内容 Contents of the invention

本发明提供了一种复合型电解质膜,其中膜内的电解质特性的均一性得到改善,并且其能以稳定的尺寸精度被制造,还提供了一种膜电极组件、一种燃料电池及用于制造它们的方法。The present invention provides a composite electrolyte membrane in which the uniformity of electrolyte characteristics in the membrane is improved and which can be manufactured with stable dimensional accuracy, a membrane electrode assembly, a fuel cell and a methods of making them.

按照本发明第一方面的用于制造复合型电解质膜的方法包括将层叠体折叠成使得所述层叠体的表面的一部分位于该表面的另一部分上的第一折叠工序,所述层叠体是通过使作为电解质层的具有电解质的电解质板片与作为加强层的包括多孔聚合物材料的加强板片层叠和一体化而获得的;使被折叠的所述层叠体的所述电解质浸渍到所述加强层中的浸渍工序;和使所述层叠体中浸渍的所述电解质水解的水解工序。The method for manufacturing a composite electrolyte membrane according to the first aspect of the present invention includes a first folding process of folding a laminate such that a part of a surface of the laminate is positioned on another part of the surface, the laminate being formed by obtained by laminating and integrating an electrolyte sheet having an electrolyte as an electrolyte layer and a reinforcing sheet including a porous polymer material as a reinforcing layer; impregnating the electrolyte of the folded laminated body to the reinforcement an impregnation step in a layer; and a hydrolysis step of hydrolyzing the electrolyte impregnated in the laminate.

此外,在按照第一方面的用于制造复合型电解质膜的方法中,在所述层叠工序中,可通过加热和层叠所述电解质板片与所述加强板片来形成所述层叠体。Furthermore, in the method for manufacturing a composite electrolyte membrane according to the first aspect, in the lamination step, the laminated body may be formed by heating and laminating the electrolyte sheet and the reinforcing sheet.

此外,在按照第一方面的用于制造复合型电解质膜的方法中,在所述浸渍工序中,可加热被折叠的所述层叠体直到所述电解质溶解,并且可使所述电解质浸渍到所述加强层中。Furthermore, in the method for producing a composite electrolyte membrane according to the first aspect, in the impregnating step, the folded laminated body may be heated until the electrolyte is dissolved, and the electrolyte may be impregnated to the in the reinforcement layer.

通过按照上述方面的用于制造复合型电解质膜的方法,包括加强层和电解质层的层叠体可在层叠工序中通过使电解质板片与加强板片借助于接合而一体化来形成。用于使两个板片层叠的方法不受特别限制,只要能形成层叠体即可,并且电解质板片的一部分可通过对电解质板片加热和加压而浸渍到加强板片的一个表面中。With the method for manufacturing a composite electrolyte membrane according to the above aspect, a laminate including the reinforcement layer and the electrolyte layer can be formed by integrating the electrolyte sheet and the reinforcement sheet by bonding in the lamination process. The method for laminating the two sheets is not particularly limited as long as a laminate can be formed, and a part of the electrolyte sheet may be impregnated into one surface of the reinforcement sheet by heating and pressing the electrolyte sheet.

此外,在所述第一折叠工序中,将层叠体折叠成使得所述层叠体的表面的一部分位于另一部分上,也就是说,在加强层侧的表面的各部分至少位于彼此上,或者在电解质层侧的表面的各部分至少位于彼此上。在折叠层叠体的工序中,通过折叠而接触的表面可通过加热和加压来接合。优选地,绕层叠体的中心轴线进行折叠,使得两个均等的表面位于彼此上,但是折叠数量和折叠方法不受特别限制,只要在施行了下述的第二折叠工序后电解质膜的两个表面上的电解质均一即可。Furthermore, in the first folding process, the laminated body is folded such that one part of the surface of the laminated body is located on another part, that is, each part of the surface on the reinforcement layer side is located at least on each other, or at least Parts of the surface on the electrolyte layer side lie at least on top of each other. In the process of folding the laminate, the surfaces that are brought into contact by folding may be bonded by heating and pressing. Preferably, the folding is performed around the central axis of the laminated body so that two equal surfaces lie on each other, but the number of foldings and the folding method are not particularly limited as long as the two sides of the electrolyte membrane are subjected to the second folding process described below. It is sufficient that the electrolyte on the surface is uniform.

在所述浸渍工序中,加热被折叠的所述层叠体至少直到所述电解质溶融,并且使所述电解质浸渍到多孔的加强层中。在该浸渍工序中,对层叠体的加压可与加热一起进行。结果,在层叠阶段采用的单个电解质板片的电解质被配置在层叠体的两个表面上。在所述水解工序中,可通过使所述层叠体中浸渍的电解质水解而赋予电解质以离子交换功能。In the impregnation process, the folded laminate is heated at least until the electrolyte melts, and the electrolyte is impregnated into the porous reinforcement layer. In this immersion process, pressurization to a laminated body may be performed together with heating. As a result, the electrolyte of the individual electrolyte sheets employed in the lamination stage is disposed on both surfaces of the stack. In the hydrolysis step, an ion exchange function can be imparted to the electrolyte by hydrolyzing the electrolyte impregnated in the laminate.

通过这种用于制造复合型电解质膜的方法,不必为将电解质板片夹在中间而在加强板片的两个表面上定位三个板片。因此,定位精度有所增加,并且电解质膜的质量得以稳定。此外,由于层叠体被折叠且单个电解质板片的电解质被浸渍,所以可在复合型电解质膜(电解质膜)的两个表面上配置均一的电解质。此外,电解质膜的厚度也得以稳定。这样,在电解质膜内电解质特性的均一性得以改善,可获得高精度的电解质膜,并且燃料电池性能可得以稳定。With this method for manufacturing a composite type electrolyte membrane, it is not necessary to position three sheets on both surfaces of the reinforcing sheet for sandwiching the electrolyte sheet. Therefore, positioning accuracy is increased, and the quality of the electrolyte membrane is stabilized. In addition, since the laminate is folded and the electrolyte of the individual electrolyte sheets is impregnated, a uniform electrolyte can be disposed on both surfaces of the composite electrolyte membrane (electrolyte membrane). In addition, the thickness of the electrolyte membrane is also stabilized. In this way, the uniformity of electrolyte characteristics is improved within the electrolyte membrane, a high-precision electrolyte membrane can be obtained, and fuel cell performance can be stabilized.

此外,如在对本发明的描述中所称的“电解质板片”和“加强板片”的形状、厚度等不受特别限制,只要它们在层叠之后可被折叠即可,其含义包括膜、薄膜等等。如本文所称,“加强板片”是由多孔聚合物材料构成的、出于加强电解质膜的目的而采用的板片,“加强层”是具有多孔聚合物材料并且出于加强电解质膜的目的而至少在电解质膜的厚度方向上形成的层,并且其含义还包括通过以电解质浸渍聚合物材料所获得的层。此外,“复合型电解质膜”是指至少包括电解质层和加强层的层,所述电解质层包括电解质,在所述加强层中多孔聚合物材料浸渍有电解质。In addition, the shape, thickness, etc. of the "electrolyte sheet" and "reinforcing sheet" as referred to in the description of the present invention are not particularly limited as long as they can be folded after lamination, and the meaning includes films, films etc. As used herein, a "reinforcing sheet" is a sheet composed of a porous polymer material for the purpose of strengthening the electrolyte membrane, and a "reinforcing layer" is a sheet of porous polymer material for the purpose of strengthening the electrolyte membrane. And at least a layer formed in the thickness direction of the electrolyte membrane, and its meaning also includes a layer obtained by impregnating a polymer material with an electrolyte. In addition, "composite type electrolyte membrane" refers to a layer including at least an electrolyte layer including an electrolyte and a reinforcement layer in which a porous polymer material is impregnated with an electrolyte.

在按照第一方面的用于制造复合型电解质膜的方法中,在所述第一折叠工序中,可将所述层叠体折叠成使得所述层叠体中在所述电解质层侧的表面的一部分位于该表面的另一部分上。按照上述方面,由于在第一折叠工序中层叠体被折叠成使得层叠体中在电解质层侧的表面的一部分位于该表面的另一部分上并且加强层侧变成电解质膜表面,所以在浸渍工序中加强层可配置在接近电解质膜的厚度方向上的表面的表面层部分中。结果,可改善在燃料电池工作时电解质膜的蠕变(creep)性能。In the method for manufacturing a composite electrolyte membrane according to the first aspect, in the first folding step, the laminated body may be folded such that a part of the surface of the laminated body on the electrolyte layer side on another part of the surface. According to the above aspect, since the laminated body is folded in the first folding process so that a part of the surface of the laminated body on the electrolyte layer side is located on the other part of the surface and the reinforcement layer side becomes the surface of the electrolyte membrane, in the dipping process The reinforcement layer may be disposed in a surface layer portion close to the surface in the thickness direction of the electrolyte membrane. As a result, the creep performance of the electrolyte membrane during fuel cell operation can be improved.

在按照第一方面的用于制造复合型电解质膜的方法中,在所述第一折叠工序中,可将所述层叠体折叠成使得所述层叠体中在所述加强层侧的表面的一部分位于该表面的另一部分上。按照上述方面,由于在第一折叠工序中层叠体被折叠成使得层叠体中在加强层侧的表面的一部分位于该表面的另一部分上并且电解质层侧变成电解质膜表面,所以在浸渍工序中电解质层形成在厚度方向上的表面层中并且加强层的位置得以稳定。结果,在配备有所述电解质膜的燃料电池中,表面层的电解质层在发电期间抑制了水移动在电解质膜的表面内的分散。此外,电解质层和催化剂层的粘附可得到改善,并且性能可得以稳定。In the method for manufacturing a composite electrolyte membrane according to the first aspect, in the first folding step, the laminated body may be folded such that a part of the surface of the laminated body on the reinforcing layer side on another part of the surface. According to the above aspect, since the laminated body is folded in the first folding process so that a part of the surface of the laminated body on the reinforcement layer side is located on the other part of the surface and the electrolyte layer side becomes the surface of the electrolyte membrane, in the dipping process The electrolyte layer is formed in the surface layer in the thickness direction and the position of the reinforcing layer is stabilized. As a result, in a fuel cell equipped with the electrolyte membrane, the electrolyte layer of the surface layer suppresses the dispersion of water movement within the surface of the electrolyte membrane during power generation. In addition, the adhesion of the electrolyte layer and the catalyst layer can be improved, and the performance can be stabilized.

任何溶融的聚合物都可用作按照上述实施例的电解质(前体聚合物),只要它未热劣化并且在水解后可赋予离子交换功能即可。可被有利地使用的聚合物的示例包括具有氟烷基醚侧链和全氟烷基主链的氟烷基共聚物的全氟质子交换树脂。具体的示例包括Nafion(商标名,Du Pont Co.制造)、Aciplex(商标名,Asahi Chemical Industry Co.,Ltd.制造)、Fremion(商标名,Asahi Glass Co.制造)和Goaselect(商标名,Japan Goatex Co.,Ltd.制造)。其它的示例包括部分氟树脂,例如三氟苯乙烯磺酸的聚合物和将磺酸基引入聚氟亚乙烯基中所获得的聚合物。也可使用其中磺酸基被引入苯乙烯-二乙烯基苯共聚物的碳氢化合物质子交换树脂、聚酰亚胺树脂等等。聚合物必须根据使用燃料电池的用途或环境来适当地选择,但是从燃料电池寿命的观点看,全氟树脂是优选的。Any molten polymer can be used as the electrolyte (precursor polymer) according to the above-described embodiments, as long as it is not thermally deteriorated and can impart an ion exchange function after hydrolysis. Examples of polymers that may be advantageously used include perfluoroproton exchange resins of fluoroalkyl copolymers having fluoroalkyl ether side chains and perfluoroalkyl backbones. Specific examples include Nafion (trade name, manufactured by Du Pont Co.), Aciplex (trade name, manufactured by Asahi Chemical Industry Co., Ltd.), Fremion (trade name, manufactured by Asahi Glass Co.), and Goaselect (trade name, manufactured by Japan manufactured by Goatex Co., Ltd.). Other examples include partial fluororesins such as polymers of trifluorostyrenesulfonic acid and polymers obtained by introducing sulfonic acid groups into polyvinylidene fluoride. Hydrocarbon proton exchange resins, polyimide resins and the like in which sulfonic acid groups are introduced into styrene-divinylbenzene copolymers can also be used. The polymer must be appropriately selected depending on the use or environment in which the fuel cell is used, but from the viewpoint of fuel cell life, perfluororesins are preferable.

加强板片在电解质浸渍工序中不溶解是必要的。包括防水聚合物的加强板片是特别优选的。包括防水聚合物的加强板片能有效地防止在固体聚合物型燃料电池中已凝结和积聚的水供给到电极反应产物。氟树脂如聚四氟乙烯(PTFE)、四氟乙烯-六氟丙烯共聚物(FEP)和四氟乙烯-全氟烷基乙烯基醚共聚物(PFA)是特别优选的,因为它们具有高防水能力。也可使用无氟膜,例如聚对苯二甲酸乙二醇酯、聚乙烯、聚丙烯和聚酰亚胺。It is essential that the reinforcing sheet does not dissolve during the electrolyte impregnation process. Reinforcement sheets comprising waterproof polymers are particularly preferred. The reinforcement sheet including the water-repellent polymer is effective in preventing water that has condensed and accumulated in the solid polymer type fuel cell from being supplied to electrode reaction products. Fluorine resins such as polytetrafluoroethylene (PTFE), tetrafluoroethylene-hexafluoropropylene copolymer (FEP) and tetrafluoroethylene-perfluoroalkyl vinyl ether copolymer (PFA) are particularly preferred because of their high water resistance ability. Fluorine-free films such as polyethylene terephthalate, polyethylene, polypropylene, and polyimide can also be used.

在按照第一方面的用于制造复合型电解质膜的方法中,当如上所述在折叠工序中将层叠体折叠成使得加强层侧的表面的一部分位于该表面的另一部分上时,在所述层叠工序中,在所述层叠体已形成后,可在所述加强层的表面上配置将过氧化氢分解成水和氧并抑制羟自由基产生的自由基抑制剂与保水材料中的至少一者。In the method for manufacturing a composite electrolyte membrane according to the first aspect, when the laminated body is folded in the folding process as described above so that a part of the surface on the reinforcing layer side is positioned on the other part of the surface, in the In the lamination step, after the laminate is formed, at least one of a radical inhibitor and a water-retaining material that decomposes hydrogen peroxide into water and oxygen and suppresses generation of hydroxyl radicals may be disposed on the surface of the reinforcing layer. By.

此外,在按照第一方面的用于制造复合型电解质膜的方法中,当如上所述在折叠工序中将层叠体折叠成使得加强层侧的表面的一部分位于该表面的另一部分上时,在所述层叠工序中,可在所述电解质板片和所述加强板片之间配置将过氧化氢分解成水和氧并抑制羟自由基产生的自由基抑制剂与保水材料中的至少一者。Furthermore, in the method for manufacturing a composite electrolyte membrane according to the first aspect, when the laminate is folded in the folding process as described above so that a part of the surface on the reinforcing layer side is located on the other part of the surface, the In the lamination process, at least one of a radical inhibitor and a water-retaining material that decomposes hydrogen peroxide into water and oxygen and suppresses generation of hydroxyl radicals may be disposed between the electrolyte sheet and the reinforcing sheet. .

按照上述方面,在第一折叠工序中,来自自由基抑制剂和保水材料之中的至少一种添加剂被夹在中间,然后在浸渍工序中添加剂在电解质膜在厚度方向上的中心被添加到电解质。因此,添加剂可被固定。According to the above aspect, in the first folding process, at least one additive from among the radical inhibitor and the water-retaining material is sandwiched, and then the additive is added to the electrolyte at the center of the electrolyte membrane in the thickness direction in the impregnating process. . Therefore, additives can be fixed.

结果,在燃料电池发电期间可防止添加剂因水的移动而移动或流出。当使用自由基抑制剂时,自由基抑制剂在水解工序中利用水在电解质膜中的移动将在燃料电池发电期间作为副产物产生的过氧化氢分解成水和氧。结果,可抑制羟自由基的产生,电解质膜得以稳定,并且可抑制其劣化。另一方面,当配置的是保水材料时,可获得其水保持和扩散效果,并且可有效地抑制由质子传导性的恶化引起的燃料电池性能的低下。As a result, the additive can be prevented from moving or flowing out due to movement of water during fuel cell power generation. When a radical inhibitor is used, the radical inhibitor decomposes hydrogen peroxide generated as a by-product during fuel cell power generation into water and oxygen by utilizing the movement of water in the electrolyte membrane in the hydrolysis process. As a result, the generation of hydroxyl radicals can be suppressed, the electrolyte membrane is stabilized, and its deterioration can be suppressed. On the other hand, when a water-retaining material is arranged, its water retention and diffusion effects can be obtained, and a decrease in fuel cell performance caused by deterioration of proton conductivity can be effectively suppressed.

在对本发明的描述中所称的自由基抑制剂是“用于将在燃料电池发电期间作为副产物产生的过氧化氢分解成水和氧并抑制羟自由基产生的材料”。其示例包括过渡金属(如铈、钌、银、钨、钯、铑、锆、钇、锰、钼、铅、钒和钛)的氧化物。保水材料不受特别限制,只要它可吸收水即可。其示例包括由吸水聚合物材料如聚苯乙烯磺酸和纤维素以及吸水无机材料如硅石和氧化钛构成的颗粒或纤维。The radical inhibitor referred to in the description of the present invention is "a material for decomposing hydrogen peroxide generated as a by-product during fuel cell power generation into water and oxygen and suppressing generation of hydroxyl radicals". Examples thereof include oxides of transition metals such as cerium, ruthenium, silver, tungsten, palladium, rhodium, zirconium, yttrium, manganese, molybdenum, lead, vanadium, and titanium. The water-retaining material is not particularly limited as long as it can absorb water. Examples thereof include particles or fibers composed of water-absorbing polymeric materials such as polystyrenesulfonic acid and cellulose, and water-absorbing inorganic materials such as silica and titanium oxide.

这种自由基抑制剂和保水材料可通过涂覆工艺如模式涂覆(diecoating)或喷涂和物理气相沉积(PVD)工艺如溅射被均一地配置在加强层的表面上。由于如上所述在第一折叠工序中自由基抑制剂和保水材料被夹在中间,所以其配置方法不受特别限制,只要它们可被夹在加强层中达到在折叠期间不会脱离的程度即可。Such radical inhibitors and water-retaining materials may be uniformly disposed on the surface of the reinforcing layer by coating processes such as diecoating or spray coating and physical vapor deposition (PVD) processes such as sputtering. Since the radical inhibitor and the water-retaining material are sandwiched in the first folding process as described above, the arrangement method thereof is not particularly limited as long as they can be sandwiched in the reinforcing layer to the extent that they will not come off during folding. Can.

当使用细粉状材料作为自由基抑制剂和保水材料时,细粉状材料的颗粒尺寸优选地大于在加强板片中形成的孔隙的孔隙尺寸。通过这样的颗粒尺寸,在第一折叠工序中粉状材料可被有利地夹在中间。When the fine powdery material is used as the radical inhibitor and water retention material, the particle size of the fine powdery material is preferably larger than the pore size of the pores formed in the reinforcing sheet. With such a particle size, the pulverulent material can advantageously be sandwiched during the first folding process.

按照本发明第二方面的用于制造膜电极组件的方法包括按照第一方面的用于制造复合型电解质膜的方法,其中,在所述层叠工序中,在所述层叠体已形成后,在所述电解质层的表面上配置阳极催化剂层和阴极催化剂层;以及在所述第一折叠工序中,将所述层叠体折叠成使得所述阳极催化剂层配置在所述层叠体的一个表面上,而所述阴极催化剂层配置在所述层叠体的另一个表面上。The method for manufacturing a membrane electrode assembly according to the second aspect of the present invention includes the method for manufacturing a composite electrolyte membrane according to the first aspect, wherein, in the lamination process, after the laminate has been formed, the an anode catalyst layer and a cathode catalyst layer are arranged on a surface of the electrolyte layer; and in the first folding step, folding the laminate such that the anode catalyst layer is arranged on one surface of the laminate, On the other hand, the cathode catalyst layer is arranged on the other surface of the laminate.

通过按照上述目的的用于制造膜电极组件的方法,由于阳极催化剂层和阴极催化剂层形成在同一表面(其中在通过层叠工序获得的层叠体中已形成电解质层)内,所以可精确地配置这些催化剂层。结果,在保持第一折叠工序中层叠体折叠位置的精度的情况下,可抑制阳极催化剂层和阴极催化剂层的相互布置的歪曲。此外,在催化剂层已形成之后可配置上述扩散层。通过采用以上述方式制造的膜电极组件,能防止在将膜电极组件组装到燃料电池中时产生组装不良,以及抑制在发电期间燃料电池性能的分散。With the method for manufacturing a membrane electrode assembly according to the above purpose, since the anode catalyst layer and the cathode catalyst layer are formed in the same surface in which the electrolyte layer has been formed in the laminate obtained by the lamination process, these can be precisely arranged catalyst layer. As a result, distortion of the mutual arrangement of the anode catalyst layer and the cathode catalyst layer can be suppressed while maintaining the accuracy of the folded position of the laminate in the first folding process. In addition, the above-mentioned diffusion layer may be disposed after the catalyst layer has been formed. By employing the membrane electrode assembly manufactured in the above manner, it is possible to prevent poor assembly from occurring when the membrane electrode assembly is assembled into a fuel cell, and to suppress dispersion of fuel cell performance during power generation.

按照本发明第三方面的用于制造膜电极组件的方法包括按照第一方面的用于制造复合型电解质膜的方法,其中,在所述层叠工序中,形成带状层叠体,并且在所述层叠体已形成后,在所述电解质层的表面上配置阳极催化剂层和阴极催化剂层,使得所述阳极催化剂层和所述阴极催化剂层沿所述层叠体的横向方向形成;以及在所述第一折叠工序中,将所述层叠体沿纵向方向折叠成使得所述阳极催化剂层配置在所述层叠体的一个表面上,而所述阴极催化剂层配置在所述层叠体的另一个表面上。The method for manufacturing a membrane electrode assembly according to the third aspect of the present invention includes the method for manufacturing a composite electrolyte membrane according to the first aspect, wherein, in the lamination step, a strip-shaped laminate is formed, and in the After the stack has been formed, disposing an anode catalyst layer and a cathode catalyst layer on the surface of the electrolyte layer such that the anode catalyst layer and the cathode catalyst layer are formed in a lateral direction of the stack; and In a folding process, the laminate is folded in the longitudinal direction such that the anode catalyst layer is arranged on one surface of the laminate and the cathode catalyst layer is arranged on the other surface of the laminate.

在按照本发明第三方面的用于制造膜电极组件的方法中,在所述层叠工序中,可将所述阳极催化剂层和所述阴极催化剂层配置成使得多个所述阳极催化剂层和多个所述阴极催化剂层沿所述纵向方向交替形成。In the method for manufacturing a membrane electrode assembly according to the third aspect of the present invention, in the stacking step, the anode catalyst layer and the cathode catalyst layer may be configured such that a plurality of the anode catalyst layers and a plurality of The cathode catalyst layers are alternately formed along the longitudinal direction.

通过按照上述方面的用于制造膜电极组件的方法,由于阳极催化剂层和阴极催化剂层沿横向方向形成在同一表面(其中在通过层叠工序获得的层叠体中已形成电解质层)内,所以可精确地配置这些催化剂层而不会有移位,以便将复合型电解质膜夹在中间。结果,在保持第一折叠工序中层叠体折叠位置的精度的情况下,可抑制阳极催化剂层和阴极催化剂层的相互布置的歪曲,可防止在将膜电极组件组装到燃料电池中时产生组装不良,以及可抑制在发电期间燃料电池性能的分散。With the method for manufacturing a membrane electrode assembly according to the above aspect, since the anode catalyst layer and the cathode catalyst layer are formed in the lateral direction in the same surface (wherein the electrolyte layer has been formed in the laminated body obtained by the lamination process), it is possible to precisely These catalyst layers are arranged without displacement so as to sandwich the composite electrolyte membrane. As a result, distortion of the mutual arrangement of the anode catalyst layer and the cathode catalyst layer can be suppressed while maintaining the accuracy of the folded position of the laminate in the first folding step, and assembly failure can be prevented when the membrane electrode assembly is assembled into a fuel cell. , and dispersion of fuel cell performance during power generation can be suppressed.

此外,由于折叠工序在将阳极催化剂层和阴极催化剂层配置成使得多个阳极催化剂层和多个阴极催化剂层沿纵向方向交替形成时进行,所以可同时制造多个带状膜电极组件。In addition, since the folding process is performed when the anode catalyst layer and the cathode catalyst layer are arranged such that a plurality of anode catalyst layers and a plurality of cathode catalyst layers are alternately formed in the longitudinal direction, a plurality of strip-shaped MEAs can be manufactured simultaneously.

按照本发明第三方面的用于制造膜电极组件的方法还可包括在所述水解工序后将所述层叠体沿所述横向方向折叠成使得所述阳极催化剂层与在所述纵向方向上邻接所述阳极催化剂层的所述阴极催化剂层彼此面对的第二折叠工序。The method for manufacturing a membrane electrode assembly according to the third aspect of the present invention may further include folding the stacked body in the transverse direction after the hydrolysis step such that the anode catalyst layer is adjacent to the anode catalyst layer in the longitudinal direction. A second folding process in which the cathode catalyst layers of the anode catalyst layers face each other.

按照本发明,通过针对由上述制造方法制造出的带状膜电极组件进行第二形成工序,可由一个膜电极组件容易地获得无移位地形成催化剂层的单个燃料电池,而不用堆叠(层叠)多个膜电极组件,如果隔板配置在面对的电极层之间的话。According to the present invention, by performing the second forming process on the belt-shaped MEA manufactured by the above-mentioned manufacturing method, a single fuel cell in which the catalyst layer is formed without displacement can be easily obtained from one MEA without stacking (stacking) A plurality of membrane electrode assemblies, if separators are arranged between facing electrode layers.

此外,由于多个阳极催化剂层和多个阴极催化剂层沿纵向方向交替地形成且因此阴极催化剂层必然形成为在纵向方向上邻接阳极催化剂层,通过进行第二折叠工序,能形成多个具有同一方向的表面的阳极催化剂层,以及形成多个具有与阳极催化剂层相反的同一方向的表面的阴极催化剂层。结果,能可靠地防止在通过典型的工艺过程层叠多个膜电极组件的情况下膜电极组件中阳极催化剂层和阴极催化剂层的组装误差。Furthermore, since a plurality of anode catalyst layers and a plurality of cathode catalyst layers are alternately formed in the longitudinal direction and thus the cathode catalyst layers are necessarily formed adjacent to the anode catalyst layer in the longitudinal direction, by performing the second folding process, a plurality of catalyst layers having the same An anode catalyst layer with a surface facing in the same direction as the anode catalyst layer, and a plurality of cathode catalyst layers having a surface opposite to the anode catalyst layer in the same direction. As a result, assembly errors of the anode catalyst layer and the cathode catalyst layer in the membrane electrode assembly can be reliably prevented in the case of laminating a plurality of membrane electrode assemblies through typical processes.

按照本发明第四方面的用于制造燃料电池的方法是包括按照第三方面的用于制造膜电极组件的方法的用于制造燃料电池的方法,并且可包括扩散层和隔板配置工序,所述扩散层和隔板配置工序在所述第二折叠工序后在所述膜电极组件的所述阳极催化剂层的表面和所述阴极催化剂层的表面上配置扩散层,以及在具有彼此相对配置的所述扩散层的所述阳极催化剂层和所述阴极催化剂层之间配置隔板,所述隔板中形成有燃料气体流路和氧气流路,使得所述燃料气体流路位于所述阳极催化剂层侧,而所述氧气流路位于所述阴极催化剂层侧。A method for manufacturing a fuel cell according to a fourth aspect of the present invention is a method for manufacturing a fuel cell including the method for manufacturing a membrane electrode assembly according to the third aspect, and may include a diffusion layer and a separator arranging process, so The diffusion layer and separator arranging step arranges a diffusion layer on the surface of the anode catalyst layer and the surface of the cathode catalyst layer of the membrane electrode assembly after the second folding step, and A separator is arranged between the anode catalyst layer and the cathode catalyst layer of the diffusion layer, and a fuel gas flow path and an oxygen flow path are formed in the separator, so that the fuel gas flow path is located between the anode catalyst layer and the anode catalyst layer. layer side, while the oxygen flow path is located on the cathode catalyst layer side.

通过按照上述方面的用于制造燃料电池的方法,隔板可配置成在第二折叠工序后朝膜电极组件的横向方向上的流动线路插入,并且可容易地获得单个燃料电池。这样,与将隔板配置在多个膜电极组件之间的典型方法相比,生产步骤的数量可减少。此外,隔板可在第二折叠工序后以连续的方式配置。因此,可抑制在获得单个燃料电池的过程中污染物的混入。With the method for manufacturing a fuel cell according to the above aspect, the separator can be configured to be inserted toward the flow line in the lateral direction of the membrane electrode assembly after the second folding process, and a single fuel cell can be easily obtained. In this way, the number of production steps can be reduced compared to a typical method of disposing separators between a plurality of membrane electrode assemblies. In addition, the separators may be arranged in a continuous manner after the second folding process. Therefore, the incorporation of pollutants in the process of obtaining a single fuel cell can be suppressed.

此外,当配置扩散层和隔板时,在膜电极组件中配置在其表面上形成有扩散层的隔板是优选的,因为扩散层和隔板可同时配置在膜电极组件中。但是,该方法不受限制,扩散层和隔板可分开配置,只要扩散层和隔板可配置在膜电极组件中并且可制造出燃料电池即可。Furthermore, when arranging the diffusion layer and the separator, it is preferable to arrange the separator having the diffusion layer formed on its surface in the membrane electrode assembly because the diffusion layer and the separator can be arranged in the membrane electrode assembly at the same time. However, the method is not limited, and the diffusion layer and the separator may be separately arranged as long as the diffusion layer and the separator can be arranged in the membrane electrode assembly and a fuel cell can be manufactured.

此外,催化剂层的配置可通过以喷涂吹送催化剂来进行,还能将催化剂层配置在底衬板片上并在加热和加压下使用工具或涂覆模将催化剂层转移到电解质层上。在使用催化剂层离聚物作为前体聚合物的情况下,可有利地制造膜电极组件,而没有后续浸渍工序中离聚物的热劣化。更为优选的是,包含在催化剂层中的电解质是含氟电解质的前体。In addition, the arrangement of the catalyst layer can be performed by blowing the catalyst by spraying, and it is also possible to arrange the catalyst layer on the substrate sheet and transfer the catalyst layer to the electrolyte layer using a tool or a coating die under heat and pressure. In the case of using a catalyst layer ionomer as a precursor polymer, a membrane electrode assembly can be advantageously manufactured without thermal degradation of the ionomer in a subsequent impregnation process. More preferably, the electrolyte contained in the catalyst layer is a precursor of a fluorine-containing electrolyte.

此外,可使用在燃料电池中通常使用的气体扩散层作为扩散层而没有特别限制。这种气体扩散层的示例包括用作包含导电物质作为主要成分的组成材料的碳纤维板片和多孔导电板片。例如为碳颗粒的导电颗粒可利用疏水树脂作为粘结材料粘结到所述板片。此外,除了具有形成在其中的气体流路之外,隔板还可适当地具有这样的结构,该结构排出在发电期间产生的水,并使冷却剂循环,以便抑制在发电期间燃料电池中的发热。In addition, a gas diffusion layer generally used in a fuel cell can be used as the diffusion layer without particular limitation. Examples of such a gas diffusion layer include a carbon fiber sheet and a porous conductive sheet used as constituent materials containing a conductive substance as a main component. Conductive particles such as carbon particles may be bonded to the sheet using a hydrophobic resin as bonding material. Furthermore, in addition to having a gas flow path formed therein, the separator may suitably have a structure that discharges water generated during power generation and circulates a coolant so as to suppress the gas flow in the fuel cell during power generation. fever.

按照本发明第五方面的复合型电解质膜至少具有电解质层和加强板片,所述电解质层包括电解质,在所述加强板片中多孔聚合物材料浸渍有所述电解质,所述复合型电解质膜至少包括:添加层,在所述添加层中,将过氧化氢分解成水和氧并抑制羟自由基产生的自由基抑制剂与保水材料中的至少一者被添加到所述电解质;形成为将所述添加层夹在中间的所述加强层;和形成在每个所述加强层的表面上的所述电解质层。The composite electrolyte membrane according to the fifth aspect of the present invention has at least an electrolyte layer and a reinforcement sheet, the electrolyte layer includes an electrolyte, and a porous polymer material is impregnated with the electrolyte in the reinforcement sheet, the composite electrolyte membrane including at least: an added layer in which at least one of a radical inhibitor that decomposes hydrogen peroxide into water and oxygen and suppresses generation of hydroxyl radicals and a water-retaining material is added to the electrolyte; formed as the reinforcing layer sandwiching the added layer; and the electrolyte layer formed on a surface of each of the reinforcing layers.

按照本发明第六方面的复合型电解质膜至少具有电解质层和加强层,所述电解质层包括电解质,在所述加强层中多孔聚合物材料浸渍有所述电解质,所述复合型电解质膜至少包括:作为所述电解质层的第一电解质层;形成为将所述第一电解质层夹在中间的添加层,在所述添加层中,将过氧化氢分解成水和氧并抑制羟自由基产生的自由基抑制剂与保水材料中的至少一者被添加到所述电解质;形成在所述添加层的表面上的所述加强层;和用作所述电解质层并形成在所述加强层的表面上的第二电解质层。The composite electrolyte membrane according to the sixth aspect of the present invention has at least an electrolyte layer and a reinforcement layer, the electrolyte layer includes an electrolyte, and a porous polymer material is impregnated with the electrolyte in the reinforcement layer, and the composite electrolyte membrane includes at least : a first electrolyte layer as the electrolyte layer; an additive layer formed to sandwich the first electrolyte layer, in which hydrogen peroxide is decomposed into water and oxygen and generation of hydroxyl radicals is suppressed At least one of a free radical inhibitor and a water-retaining material is added to the electrolyte; the reinforcement layer is formed on the surface of the added layer; and the reinforcement layer is used as the electrolyte layer and is formed on the reinforcement layer A second electrolyte layer on the surface.

通过按照上述方面的复合型电解质膜,通过如上所述形成添加有选自自由基抑制剂和保水材料之中的至少一种添加剂的添加层,能抑制在燃料电池发电期间在水移动时这些材料的移动和流动损失。With the composite electrolyte membrane according to the above aspect, by forming the additive layer to which at least one additive selected from radical inhibitors and water-retaining materials is added as described above, these materials can be suppressed when water moves during fuel cell power generation. movement and flow losses.

按照本发明第七方面的复合型电解质膜至少包括一对阳极催化剂层和阴极催化剂层,所述阳极催化剂层和阴极催化剂层配置在复合型电解质膜的两个表面上,以使得所述阳极催化剂层和所述阴极催化剂层将所述复合型电解质膜夹在中间,在所述复合型电解质膜中,包括多孔聚合物材料的加强板片浸渍有包括电解质的电解质板片,其中,所述膜电极组件是带状膜电极组件,并且多个所述阳极催化剂层和多个所述阴极催化剂层在所述膜电极组件的表面上沿纵向方向交替形成。The composite electrolyte membrane according to the seventh aspect of the present invention includes at least a pair of anode catalyst layer and cathode catalyst layer, and the anode catalyst layer and the cathode catalyst layer are arranged on both surfaces of the composite electrolyte membrane, so that the anode catalyst layer layer and the cathode catalyst layer sandwich the composite electrolyte membrane in which a reinforcement sheet comprising a porous polymer material is impregnated with an electrolyte sheet comprising an electrolyte, wherein the membrane The electrode assembly is a strip-shaped membrane electrode assembly, and a plurality of the anode catalyst layers and a plurality of the cathode catalyst layers are alternately formed on the surface of the membrane electrode assembly in a longitudinal direction.

按照本发明第八方面的复合型电解质膜至少具有一对阳极催化剂层和阴极催化剂层,所述阳极催化剂层和阴极催化剂层配置在按照第五方面的复合型电解质膜的两个表面上,以便将所述复合型电解质膜夹在中间,其中,所述膜电极组件是带状膜电极组件,并且所述阳极催化剂层和所述阴极催化剂层在所述膜电极组件的表面上沿纵向方向交替形成。The composite electrolyte membrane according to the eighth aspect of the present invention has at least a pair of anode catalyst layer and cathode catalyst layer arranged on both surfaces of the composite electrolyte membrane according to the fifth aspect, so that Sandwiching the composite electrolyte membrane, wherein the membrane electrode assembly is a belt-shaped membrane electrode assembly, and the anode catalyst layers and the cathode catalyst layers are alternated in the longitudinal direction on the surface of the membrane electrode assembly form.

按照本发明第九方面的复合型电解质膜至少具有一对阳极催化剂层和阴极催化剂层,所述阳极催化剂层和阴极催化剂层配置在按照第六方面的复合型电解质膜的两个表面上,以便将所述复合型电解质膜夹在中间,其中,所述膜电极组件是带状膜电极组件,并且所述阳极催化剂层和所述阴极催化剂层在所述膜电极组件的表面上沿纵向方向交替形成。The composite electrolyte membrane according to the ninth aspect of the present invention has at least a pair of anode catalyst layer and cathode catalyst layer arranged on both surfaces of the composite electrolyte membrane according to the sixth aspect, so that Sandwiching the composite electrolyte membrane, wherein the membrane electrode assembly is a belt-shaped membrane electrode assembly, and the anode catalyst layers and the cathode catalyst layers are alternated in the longitudinal direction on the surface of the membrane electrode assembly form.

通过上述方面的膜电极组件,由于多个阳极催化剂层和多个阴极催化剂层沿纵向方向形成在膜电极组件的表面上,所以膜电极组件可沿横向方向折叠成使得所述阳极催化剂层与在所述纵向方向上邻接所述阳极催化剂层的所述阴极催化剂层彼此面对。以上述方式折叠的膜电极组件在其中形成有多个具有同一方向的表面的阳极催化剂层和多个具有与阳极催化剂层的方向相反的同一方向的表面的阴极催化剂层。With the membrane electrode assembly of the above aspect, since a plurality of anode catalyst layers and a plurality of cathode catalyst layers are formed on the surface of the membrane electrode assembly in the longitudinal direction, the membrane electrode assembly can be folded in the lateral direction so that the anode catalyst layers are The cathode catalyst layers adjacent to the anode catalyst layer in the longitudinal direction face each other. The membrane electrode assembly folded in the above manner has formed therein a plurality of anode catalyst layers having surfaces in the same direction and a plurality of cathode catalyst layers having surfaces in the same direction opposite to the direction of the anode catalyst layer.

按照第七至第九方面的膜电极组件可沿横向方向折叠成使得所述阳极催化剂层与在所述纵向方向上邻接所述阳极催化剂层的所述阴极催化剂层彼此面对。The membrane electrode assembly according to the seventh to ninth aspects may be folded in the lateral direction such that the anode catalyst layer and the cathode catalyst layer adjacent to the anode catalyst layer in the longitudinal direction face each other.

按照上述方面的膜电极组件具有这样的结构,该结构在其中形成有多个具有同一方向的表面的阳极催化剂层和多个具有与阳极催化剂层的方向相反的同一方向的表面的阴极催化剂层。因此,通过在膜电极组件的折叠部分中配置扩散层和隔板,能容易地制造燃料电池且没有相关技术通常存在的膜电极组件的组装不良。The membrane electrode assembly according to the above aspect has a structure in which a plurality of anode catalyst layers having surfaces in the same direction and a plurality of cathode catalyst layers having surfaces in the same direction opposite to that of the anode catalyst layers are formed therein. Therefore, by arranging the diffusion layer and the separator in the folded portion of the membrane electrode assembly, the fuel cell can be easily manufactured without poor assembly of the membrane electrode assembly generally present in the related art.

按照本发明第十方面的燃料电池包括按照第九方面的膜电极组件,该燃料电池包括:所述膜电极组件;扩散层,所述扩散层配置在所述膜电极组件的所述阳极催化剂层的表面和所述阴极催化剂层的表面上;和隔板,所述隔板中至少形成有位于所述阳极催化剂层侧的燃料气体流路和位于所述阴极催化剂层侧的氧气流路,并且所述隔板配置在具有彼此相对配置的所述扩散层的所述阳极催化剂层和所述阴极催化剂层之间。按照该方面,可通过切断沿膜电极组件的纵向方向折叠的部分(电解质膜的连接各单个燃料电池的部分)获得期望数量的燃料电池。A fuel cell according to a tenth aspect of the present invention includes the membrane electrode assembly according to the ninth aspect, the fuel cell comprising: the membrane electrode assembly; a diffusion layer arranged on the anode catalyst layer of the membrane electrode assembly and the surface of the cathode catalyst layer; and a separator in which at least a fuel gas flow path on the anode catalyst layer side and an oxygen flow path on the cathode catalyst layer side are formed, and The separator is disposed between the anode catalyst layer and the cathode catalyst layer having the diffusion layers disposed opposite to each other. According to this aspect, a desired number of fuel cells can be obtained by cutting off the portion folded in the longitudinal direction of the membrane electrode assembly (the portion of the electrolyte membrane connecting individual fuel cells).

按照本发明,可获得一种具有稳定尺寸精度的复合型电解质膜,其中膜内的电解质特性的均一性得到改善。此外,能获得这样一种膜电极组件,其中阳极催化剂层和阴极催化剂层被形成为无移位地形成复合型电解质膜。此外,可容易地获得无污染物的期望数量的燃料电池。According to the present invention, it is possible to obtain a composite electrolyte membrane having stable dimensional accuracy in which the uniformity of electrolyte characteristics within the membrane is improved. Furthermore, it is possible to obtain a membrane electrode assembly in which the anode catalyst layer and the cathode catalyst layer are formed so as to form a composite type electrolyte membrane without displacement. Furthermore, a desired number of fuel cells free from pollutants can be easily obtained.

附图说明 Description of drawings

从下面参照附图对优选实施例的说明中可更清楚地看到本发明的上述和/或其它目的、特征及优点,在附图中相似的附图标记用于表示相似的元件,并且其中:The above and/or other objects, features and advantages of the present invention will become more apparent from the following description of preferred embodiments with reference to the accompanying drawings, in which like reference numerals are used for like elements, and wherein :

图1是示出本发明第一实施例的用于制造复合型电解质膜的方法的示意图;1 is a schematic diagram showing a method for manufacturing a composite electrolyte membrane according to a first embodiment of the present invention;

图2是用于实施图1所示的制造方法的制造设备的示意图;Figure 2 is a schematic diagram of a manufacturing facility for implementing the manufacturing method shown in Figure 1;

图3是示出本发明第二实施例的用于制造复合型电解质膜的方法的示意图;3 is a schematic diagram showing a method for manufacturing a composite electrolyte membrane according to a second embodiment of the present invention;

图4是示出本发明第三实施例的用于制造复合型电解质膜的方法的示意图;4 is a schematic diagram showing a method for manufacturing a composite electrolyte membrane according to a third embodiment of the present invention;

图5是示出本发明第四实施例的用于制造复合型电解质膜的方法的示意图;5 is a schematic diagram showing a method for manufacturing a composite electrolyte membrane according to a fourth embodiment of the present invention;

图6是用于实施图5所示的制造方法的制造设备的示意图;6 is a schematic diagram of a manufacturing facility for implementing the manufacturing method shown in FIG. 5;

图7是示出本发明第五实施例的用于制造复合型电解质膜的方法的示意图;7 is a schematic diagram showing a method for manufacturing a composite electrolyte membrane according to a fifth embodiment of the present invention;

图8是示出本发明第六实施例的用于制造复合型电解质膜的方法的示意图;8 is a schematic diagram showing a method for manufacturing a composite electrolyte membrane according to a sixth embodiment of the present invention;

图9是示出本发明一个实施例的用于制造膜电极组件的方法的示意图;9 is a schematic diagram illustrating a method for manufacturing a membrane electrode assembly according to an embodiment of the present invention;

图10示出图9所示的膜电极组件的第二折叠;Figure 10 shows a second fold of the membrane electrode assembly shown in Figure 9;

图11示出用于从图10所示的膜电极组件制造燃料电池的方法;Figure 11 shows a method for fabricating a fuel cell from the membrane electrode assembly shown in Figure 10;

图12示出用于从由图11所示的方法制造的燃料电池制造具有期望数量的单元电池的燃料电池的方法;FIG. 12 shows a method for manufacturing a fuel cell having a desired number of unit cells from the fuel cell manufactured by the method shown in FIG. 11;

图13A示出在按照相关技术的用于制造复合型电解质膜的方法中用于通过流延膜形成方法制造复合型电解质膜的方法;13A shows a method for manufacturing a composite electrolyte membrane by a casting film forming method in a method for manufacturing a composite electrolyte membrane according to the related art;

图13B示出在按照相关技术的用于制造复合型电解质膜的方法中用于通过转移工序在复合型电解质膜上形成催化剂层的方法;以及13B shows a method for forming a catalyst layer on a composite electrolyte membrane through a transfer process in a method for manufacturing a composite electrolyte membrane according to the related art; and

图14是示出按照相关技术的固体聚合物型燃料电池(单个电池)的示例的示意图。Fig. 14 is a schematic diagram showing an example of a solid polymer type fuel cell (single cell) according to the related art.

具体实施方式 Detailed ways

下面将参照附图对本发明的具体实施例进行描述。Specific embodiments of the present invention will be described below with reference to the accompanying drawings.

图1是示出第一实施例的用于制造复合型电解质膜(电解质膜)的方法的示意图,图2是用于实施图1所示的制造方法的制造设备的示意图。1 is a schematic diagram showing a method for manufacturing a composite electrolyte membrane (electrolyte membrane) of a first embodiment, and FIG. 2 is a schematic diagram of a manufacturing facility for implementing the manufacturing method shown in FIG. 1 .

如图1和图2所示,首先,准备由带状电解质构成的板片(电解质板片)11和由为多孔聚合物材料的聚四氟乙烯(PTFE)构成的带状加强板片12,并实行层叠工序。更具体地,在层叠工序中,电解质板片11和加强板片12被加热和层叠并制造出层叠体10A,其中电解质板片用作电解质层11a,而加强板片12用作加强层12a。As shown in Figures 1 and 2, at first, prepare a sheet (electrolyte sheet) 11 made of a strip-shaped electrolyte and a strip-shaped reinforcing sheet 12 made of polytetrafluoroethylene (PTFE) which is a porous polymer material, And implement the lamination process. More specifically, in the lamination process, the electrolyte sheet 11 and the reinforcement sheet 12 are heated and laminated to produce a laminate 10A in which the electrolyte sheet serves as the electrolyte layer 11a and the reinforcement sheet 12 serves as the reinforcement layer 12a.

用于使两个板片层叠的方法可通过粘贴或浸渍来实施。更具体地,如图2所示,例如,通过在一对辊子31a、31b之间对电解质板片11和加强板片12一起加热和加压,能将电解质板片的一部分浸渍到加强板片12的一个表面中。在该工序中进行的加热的温度优选地在100至280℃的范围内。结果,可使电解质板片11和加强板片12一体化。可使用溶融的电解质来代替电解质板片11。The method for laminating the two sheets can be carried out by gluing or dipping. More specifically, as shown in FIG. 2, for example, by heating and pressing the electrolyte sheet 11 and the reinforcement sheet 12 together between a pair of rollers 31a, 31b, a part of the electrolyte sheet can be impregnated into the reinforcement sheet. 12 in one surface. The temperature of the heating performed in this process is preferably in the range of 100 to 280°C. As a result, the electrolyte sheet 11 and the reinforcement sheet 12 can be integrated. Instead of the electrolyte sheet 11, molten electrolyte may be used.

然后,对在层叠工序中制造出的层叠体10A进行折叠。更具体地,沿层叠体10A的中心线L在中央部折叠层叠体10A,使得层叠体10A的在加强层12a一侧的前表面(加强层表面)的一部分位于该前表面的另一部分上,由此制造出层叠体10B。Then, the laminated body 10A produced in the laminating step is folded. More specifically, the laminated body 10A is folded at the central portion along the center line L of the laminated body 10A so that a part of the front surface (reinforcement layer surface) of the laminated body 10A on the reinforcing layer 12a side is positioned on the other part of the front surface, Thus, a laminated body 10B was manufactured.

更具体地,如图2所示,可通过具有V形的凸部和凹部并沿层叠体10A的传送方向(MD方向)旋转的辊子32a、32b在层叠体10A的横向方向上的中心折叠层叠体10A。然后,利用辊子33a、33b变形为V形形状的层叠体10A被进一步折叠成使得层叠体10A的加强层12a的一部分位于另一部分上,并且通过用辊子33a、33b加热和加压使加强层12a的表面接合。在该工序中加热层叠体10A的温度优选地在100至280℃的范围内。More specifically, as shown in FIG. 2 , the laminate can be folded at the center in the transverse direction of the laminated body 10A by rollers 32 a, 32 b having V-shaped protrusions and recesses and rotating in the transport direction (MD direction) of the laminated body 10A. Body 10A. Then, the laminated body 10A deformed into a V-shape by the rollers 33a, 33b is further folded such that a part of the reinforcing layer 12a of the laminated body 10A is positioned on the other part, and the reinforcing layer 12a is formed by heating and pressing with the rollers 33a, 33b. surface bonding. The temperature for heating the laminated body 10A in this process is preferably in the range of 100 to 280°C.

然后,在折叠工序中制造出的层叠体10B由辊子34a、34b转过90°,并且层叠体10B被浸渍。更具体地,对层叠体10B加热和加压直到电解质溶融,并且将电解质浸渍到加强层12a中,以制造层叠体10C。Then, the laminated body 10B produced in the folding process is turned by 90° by the rollers 34a, 34b, and the laminated body 10B is dipped. More specifically, the laminated body 10B is heated and pressurized until the electrolyte is melted, and the electrolyte is impregnated into the reinforcement layer 12a to manufacture the laminated body 10C.

更具体地,如图2所示,层叠体10B的表面上的电解质层11a的电解质可浸渍到多孔加强层12a的孔隙中,并且可利用沿层叠体10B的传送方向旋转的加热和加压辊子35a、35b获得浸渍有电解质的加强层12b。在该工序中加热层叠体10B的温度优选地在200至280℃的范围内。More specifically, as shown in FIG. 2, the electrolyte of the electrolyte layer 11a on the surface of the laminated body 10B may be impregnated into the pores of the porous reinforcing layer 12a, and heating and pressing rollers rotating in the conveyance direction of the laminated body 10B may be used. 35a, 35b obtain the reinforcing layer 12b impregnated with electrolyte. The temperature for heating the laminated body 10B in this process is preferably in the range of 200 to 280°C.

可使在浸渍工序中制造出的层叠体10C进行水解,可赋予层叠体10C以离子交换功能,并且可获得复合型电解质膜100A。如图2所示,在水解工序后,可使复合型电解质膜100A干燥,并且可利用卷绕装置(图中未示出)卷绕板片状的复合型电解质膜100A。The laminate 10C produced in the immersion step can be hydrolyzed, the ion exchange function can be imparted to the laminate 10C, and the composite electrolyte membrane 100A can be obtained. As shown in FIG. 2 , after the hydrolysis step, the composite electrolyte membrane 100A can be dried, and the plate-shaped composite electrolyte membrane 100A can be wound by a winding device (not shown).

由此获得的复合型电解质膜100A仅由两个板片制造而成:电解质板片11和加强板片12。因此,可容易地排布所述板片,并且电解质膜的质量得以稳定。此外,层叠体10A可被折叠并且一个电解质板片11的电解质可被浸渍。结果,构成同一电解质板片11的均一电解质配置在复合型电解质膜100A的两个表面上,并且电解质膜的厚度也得到稳定。这样,能改善电解质膜内电解质特性的均一性,获得高精度的电解质膜,并稳定燃料电池的性能。The composite electrolyte membrane 100A thus obtained is manufactured from only two sheets: the electrolyte sheet 11 and the reinforcing sheet 12 . Therefore, the sheets can be easily arranged, and the quality of the electrolyte membrane can be stabilized. Furthermore, the laminated body 10A may be folded and the electrolyte of one electrolyte sheet 11 may be impregnated. As a result, a uniform electrolyte constituting the same electrolyte sheet 11 is arranged on both surfaces of the composite electrolyte membrane 100A, and the thickness of the electrolyte membrane is also stabilized. In this way, the uniformity of the electrolyte characteristics in the electrolyte membrane can be improved, a high-precision electrolyte membrane can be obtained, and the performance of the fuel cell can be stabilized.

此外,折叠工序被进行成使得在加强层12a一侧的表面(加强层表面)的一部分位于另一部分上,并且在电解质层11a一侧的表面(电解质表面)变成层叠体10B的前表面。因此,在浸渍工序中,电解质层11a形成在厚度方向上的表面层中,并且加强层12a的位置得以稳定。结果,在配备有电解质膜100A的燃料电池中,在发电期间在电解质膜100A的表面内水移动的分散由表面层的电解质层11a抑制。此外,可改善电解质膜100A与催化剂层(图中未示出)的粘附,并且燃料电池性能可得以稳定。Further, the folding process is performed so that a part of the surface on the reinforcing layer 12a side (reinforcement layer surface) is positioned on the other part, and the surface on the electrolyte layer 11a side (electrolyte surface) becomes the front surface of the laminated body 10B. Therefore, in the impregnation process, the electrolyte layer 11a is formed in the surface layer in the thickness direction, and the position of the reinforcement layer 12a is stabilized. As a result, in the fuel cell equipped with the electrolyte membrane 100A, dispersion of water movement within the surface of the electrolyte membrane 100A during power generation is suppressed by the electrolyte layer 11 a of the surface layer. In addition, adhesion of the electrolyte membrane 100A to a catalyst layer (not shown in the figure) can be improved, and fuel cell performance can be stabilized.

此外,在通过图2所示的制造方法制造复合型电解质膜100A的情况下,可仅通过使两个构件接合执行层叠工序,并且从层叠工序到水解工序的操作可实施为连续的程序。因此,可简化工序,有利于质量控制,并且可提高生产率。Furthermore, in the case of manufacturing the composite electrolyte membrane 100A by the manufacturing method shown in FIG. 2 , the lamination process can be performed only by joining two members, and the operations from the lamination process to the hydrolysis process can be implemented as a continuous procedure. Therefore, the process can be simplified, quality control can be facilitated, and productivity can be improved.

图3示出按照本发明的用于制造复合型电解质膜的方法的第二实施例。该实施例与图1所示的第一实施例的不同之处在于配置有催化剂层13a、13b。图3示出了形成膜电极组件(MEA)50A的催化剂层之前的工序。第二实施例的制造方法包括上述的层叠工序、折叠工序、浸渍工序和水解工序,这些工序采用相同的附图标记并省略其详细说明。FIG. 3 shows a second embodiment of the method for manufacturing a composite electrolyte membrane according to the present invention. This embodiment differs from the first embodiment shown in FIG. 1 in that catalyst layers 13a, 13b are provided. FIG. 3 shows the process before forming the catalyst layer of the membrane electrode assembly (MEA) 50A. The manufacturing method of the second embodiment includes the above-mentioned lamination process, folding process, dipping process, and hydrolysis process, and the same reference numerals are used for these processes and detailed description thereof will be omitted.

如图3所示,在层叠工序中,使电解质板片11与加强板片12接合和层叠,并制造出由电解质层11a和加强层12a构成的层叠体10A。然后,在层叠体10A已形成后,将阳极催化剂层13a和阴极催化剂层13b配置在电解质层11a的表面上,并制造出其上形成有催化剂层13a、13b的层叠体10D。As shown in FIG. 3 , in the lamination step, the electrolyte sheet 11 and the reinforcement sheet 12 are bonded and laminated to manufacture a laminate 10A composed of the electrolyte layer 11 a and the reinforcement layer 12 a. Then, after laminate 10A has been formed, anode catalyst layer 13a and cathode catalyst layer 13b are arranged on the surface of electrolyte layer 11a, and laminate 10D on which catalyst layers 13a, 13b are formed is manufactured.

更具体地,在催化剂配置工序中,可通过利用喷射器吹送催化剂来配置催化剂层13a、13b,或者可将催化剂层配置在底衬板片上,然后可通过利用工具或涂覆模加热和加压将催化剂层转移到电解质层上。利用催化剂层离聚物作为前体聚合物的优点在于能防止离聚物在后续浸渍工序中的离聚物热劣化。More specifically, in the catalyst disposing process, the catalyst layers 13a, 13b may be disposed by blowing the catalyst with an injector, or the catalyst layer may be disposed on the substrate sheet, and then may be heated and pressurized by using a tool or a coating die. The catalyst layer is transferred onto the electrolyte layer. The advantage of using the catalyst layer ionomer as the precursor polymer is that it can prevent the thermal degradation of the ionomer in the subsequent impregnation process.

然后,在折叠工序中,将层叠体10D折叠成使得阳极催化剂层13a配置在层叠体10E的一个表面上,而阴极催化剂层13b配置在层叠体10E的另一个表面上。在后续的浸渍工序中,使电解质浸渍到加强层12a中,并制造出层叠体10F。在水解工序中,赋予层叠体10F的电解质以离子交换功能,并且可获得包括复合型电解质膜100B的膜电极组件50A。Then, in the folding process, the laminated body 10D is folded such that the anode catalyst layer 13a is arranged on one surface of the laminated body 10E, and the cathode catalyst layer 13b is arranged on the other surface of the laminated body 10E. In the subsequent impregnation step, the electrolyte is impregnated into the reinforcement layer 12 a to manufacture the laminated body 10F. In the hydrolysis process, an ion exchange function is imparted to the electrolyte of the laminate 10F, and a membrane electrode assembly 50A including the composite electrolyte membrane 100B can be obtained.

通过上述的用于制造复合型电解质膜100B和膜电极组件50A的方法,阳极催化剂层13a和阴极催化剂层13b形成于在层叠工序中获得的层叠体10A的已形成了电解质层11a的同一表面内。因此,催化剂层13a、13b可精确地定位。结果,在可保持折叠工序中层叠体10D的折叠位置的精度的情况下,能抑制阳极催化剂层13a和阴极催化剂层13b的移位。By the method for manufacturing the composite electrolyte membrane 100B and the membrane electrode assembly 50A described above, the anode catalyst layer 13a and the cathode catalyst layer 13b are formed in the same surface of the laminated body 10A obtained in the lamination process on which the electrolyte layer 11a has been formed. . Therefore, the catalyst layers 13a, 13b can be precisely positioned. As a result, displacement of the anode catalyst layer 13 a and the cathode catalyst layer 13 b can be suppressed while the accuracy of the folding position of the laminate 10D in the folding process can be maintained.

通过在燃料电池中采用包括以上述方式制造的电解质膜100B的膜电极组件50A,能防止在将膜组装为燃料电池的单元电池时产生组装不良,以及抑制发电期间燃料电池性能的分散。特别地,由于表面层的电解质层11a以良好的稳定性形成,所以可改善电解质层11a与催化剂层13a、13b的粘附。By employing the membrane electrode assembly 50A including the electrolyte membrane 100B manufactured in the above manner in a fuel cell, it is possible to prevent poor assembly when the membrane is assembled into a unit cell of the fuel cell, and to suppress dispersion of fuel cell performance during power generation. In particular, since the electrolyte layer 11a of the surface layer is formed with good stability, the adhesion of the electrolyte layer 11a to the catalyst layers 13a, 13b can be improved.

图4示出按照本发明的用于制造复合型电解质膜的方法的第三实施例。第三实施例的制造方法与图1所示的第一实施例的不同之处在于,在折叠工序中折叠方向不同。第三实施例的制造方法包括上述的层叠工序、浸渍工序和水解工序,这些工序采用相同的附图标记并省略其详细说明。FIG. 4 shows a third embodiment of the method for manufacturing a composite electrolyte membrane according to the present invention. The manufacturing method of the third embodiment differs from that of the first embodiment shown in FIG. 1 in that the folding direction is different in the folding process. The manufacturing method of the third embodiment includes the above-mentioned lamination process, dipping process, and hydrolysis process, and the same reference numerals are used for these processes and detailed description thereof will be omitted.

如图4所示,在层叠工序中,使电解质板片11与加强板片12接合和层叠,并制造出由电解质层11a和加强层12a构成的层叠体10A。然后,对在层叠工序中制造出的层叠体10A进行折叠工序。更具体地,沿层叠体10A的中心线L在中央部将层叠体10A折叠成使得层叠体10A的在电解质层11a一侧的前表面(电解质层表面)的一部分位于该前表面的另一部分上,由此制造出层叠体10G。As shown in FIG. 4 , in the lamination process, the electrolyte sheet 11 and the reinforcement sheet 12 are bonded and laminated to manufacture a laminate 10A composed of the electrolyte layer 11 a and the reinforcement layer 12 a. Then, the folding process is performed on the laminated body 10A produced in the laminating process. More specifically, the laminated body 10A is folded at the central portion along the center line L of the laminated body 10A so that a part of the front surface (electrolyte layer surface) of the laminated body 10A on the side of the electrolyte layer 11a is positioned on the other part of the front surface. , thereby manufacturing a laminated body 10G.

然后,在浸渍工序中,使电解质浸渍到加强层12a中并制造出层叠体10H。在水解工序中,赋予层叠体10H的电解质以离子交换功能,并且可获得复合型电解质膜100C。Then, in the impregnation step, the reinforcement layer 12 a is impregnated with an electrolyte to manufacture a laminated body 10H. In the hydrolysis step, an ion exchange function is imparted to the electrolyte of the laminate 10H, and a composite electrolyte membrane 100C can be obtained.

通过上述的用于制造复合型电解质膜100C的方法,层叠体10A在下面的工序中被折叠成使得电解质层11a的表面的一部分位于另一部分上,并且加强层12a变成电解质膜的表面。因此,电解质层11b形成在复合型电解质膜100C的厚度方向上的中心,并且浸渍有电解质的加强层12b可配置在靠近电解质膜的厚度方向上的表面的表面层部分中。结果,可改善燃料电池工作过程中电解质膜100C的蠕变性能。With the method for manufacturing composite electrolyte membrane 100C described above, laminated body 10A is folded in the following process so that one part of the surface of electrolyte layer 11a lies on the other, and reinforcement layer 12a becomes the surface of the electrolyte membrane. Accordingly, the electrolyte layer 11b is formed at the center in the thickness direction of the composite electrolyte membrane 100C, and the reinforcement layer 12b impregnated with electrolyte may be arranged in a surface layer portion close to the surface in the thickness direction of the electrolyte membrane. As a result, the creep performance of the electrolyte membrane 100C during operation of the fuel cell can be improved.

图5示出按照本发明的用于制造复合型电解质膜的方法的第四实施例。图6是用于实施图5所示的制造方法的制造设备的示意图。第四实施例的制造方法与第一实施例的不同之处在于,在层叠工序后配置保水材料。第四实施例的制造方法包括上述的层叠工序、浸渍工序和水解工序,这些工序采用相同的附图标记并省略其详细说明。FIG. 5 shows a fourth embodiment of the method for manufacturing a composite electrolyte membrane according to the present invention. FIG. 6 is a schematic diagram of a manufacturing facility for implementing the manufacturing method shown in FIG. 5 . The manufacturing method of the fourth embodiment is different from that of the first embodiment in that the water-retaining material is disposed after the lamination process. The manufacturing method of the fourth embodiment includes the above-mentioned lamination process, dipping process, and hydrolysis process, and the same reference numerals are used for these processes and detailed description thereof will be omitted.

如图5所示,在层叠工序中,使电解质板片11与加强板片12接合和层叠,并制造出由电解质层11a和加强层12a构成的层叠体10A。在随后的保水材料配置工序中,在层叠体10A已形成后将保水材料14配置在加强层12a的表面上。更具体地,如图6所示,通过涂覆工艺如模式涂覆或喷涂或者通过溅射来将保水材料14涂覆到加强层12a的表面上,使得保水材料均一地配置在其上。这样,由于保水材料在下述的折叠工序中被夹在加强层之间,所以保水材料被牢固地粘附以防止其在折叠期间脱离是优选的。当使用细粉状的材料作为保水材料时,由于其被夹在中间,所以如上所述,在折叠期间,保水材料的颗粒尺寸大于在加强板片中形成的孔隙的直径是优选的。As shown in FIG. 5 , in the lamination step, the electrolyte sheet 11 and the reinforcement sheet 12 are bonded and laminated to manufacture a laminate 10A composed of the electrolyte layer 11 a and the reinforcement layer 12 a. In the subsequent water-retaining material arrangement process, the water-retaining material 14 is arranged on the surface of the reinforcement layer 12a after the laminated body 10A has been formed. More specifically, as shown in FIG. 6, the water-retaining material 14 is coated on the surface of the reinforcement layer 12a by a coating process such as pattern coating or spraying or by sputtering so that the water-retaining material is uniformly disposed thereon. In this way, since the water-retaining material is sandwiched between reinforcing layers in a folding process described later, it is preferable that the water-retaining material is firmly adhered to prevent it from coming off during folding. When a finely powdered material is used as the water-retaining material, since it is sandwiched, it is preferable that the particle size of the water-retaining material is larger than the diameter of pores formed in the reinforcement sheet during folding as described above.

然后,在折叠工序中,保水材料14被夹在加强层12a之间,从而加强层侧的表面的一部分位于另一部分上,层叠体10I被折叠,并且制造出层叠体10J。在浸渍工序中,使电解质层11a的电解质浸渍到保水材料14和加强层12a中,并制造出层叠体10K。在水解工序中,使层叠体10K的电解质水解以赋予其离子交换功能,并获得复合型电解质膜100D。Then, in the folding process, the water retaining material 14 is sandwiched between the reinforcing layers 12a so that one part of the surface on the reinforcing layer side is positioned on the other, the laminated body 10I is folded, and a laminated body 10J is manufactured. In the immersion step, the electrolyte of the electrolyte layer 11a is impregnated into the water-retaining material 14 and the reinforcement layer 12a to manufacture a laminated body 10K. In the hydrolysis step, the electrolyte of the laminate 10K is hydrolyzed to impart an ion exchange function thereto, and a composite electrolyte membrane 100D is obtained.

这样,如图5所示,可获得复合型电解质膜100D,其至少包括其中保水材料14作为添加剂被添加到电解质的添加层14b、形成为将添加层14b夹在中间并浸渍有电解质的加强层12b和形成在加强层12b的表面上的电解质层11a,前述层沿膜的厚度方向堆叠。In this way, as shown in FIG. 5 , a composite electrolyte membrane 100D including at least an additive layer 14b in which a water-retaining material 14 is added to the electrolyte as an additive, a reinforcement layer formed to sandwich the additive layer 14b and impregnated with electrolyte can be obtained. 12b and the electrolyte layer 11a formed on the surface of the reinforcing layer 12b, the foregoing layers being stacked in the thickness direction of the membrane.

在以上述方式制造的复合型电解质膜100D中,在折叠期间保水材料14作为添加剂被夹在中间,由此能将保水材料固定在电解质膜100D的厚度方向上的中心。结果,可防止保水材料14在水移动的作用下移动,并且可抑制在燃料电池发电期间的流动损失。结果,可确保稳定的质子传导性。In the composite electrolyte membrane 100D manufactured in the above manner, the water retaining material 14 is sandwiched as an additive during folding, whereby the water retaining material can be fixed at the center in the thickness direction of the electrolyte membrane 100D. As a result, the water retaining material 14 can be prevented from moving due to water movement, and flow loss during fuel cell power generation can be suppressed. As a result, stable proton conductivity can be ensured.

图7示出按照本发明的用于制造复合型电解质膜的方法的第五实施例。第五实施例的制造方法与第四实施例的不同之处在于,在层叠工序中存在催化剂层。第五实施例的制造方法包括上述的浸渍工序、折叠工序和水解工序,这些工序采用相同的附图标记并省略其详细说明。FIG. 7 shows a fifth embodiment of the method for manufacturing a composite electrolyte membrane according to the present invention. The manufacturing method of the fifth embodiment differs from the fourth embodiment in that a catalyst layer is present in the lamination process. The manufacturing method of the fifth embodiment includes the above-mentioned dipping process, folding process, and hydrolysis process, and these processes use the same reference numerals and their detailed descriptions are omitted.

如图7所示,在层叠工序中,使电解质板片11与加强板片12接合和层叠。同时,配置在底衬板片81上的阳极催化剂层13a和阴极催化剂层13b从位于电解质板片11另一侧的表面进行配置并制造出层叠体10L。As shown in FIG. 7 , in the lamination process, the electrolyte sheet 11 and the reinforcement sheet 12 are bonded and laminated. Simultaneously, the anode catalyst layer 13a and the cathode catalyst layer 13b arranged on the backing sheet 81 are arranged from the surface on the other side of the electrolyte sheet 11 to manufacture a laminated body 10L.

然后,可通过保水材料配置工序、折叠工序、浸渍工序和水解工序获得包括复合型电解质膜100E的膜电极组件50B。在这种情况下,在浸渍工序后将底衬板片81从层叠体10K移除,在水解工序后赋予层叠体10K的电解质以离子交换功能,并且可获得包括复合型电解质膜100E的膜电极组件50B。Then, the membrane electrode assembly 50B including the composite electrolyte membrane 100E can be obtained through a water-retaining material arrangement process, a folding process, an impregnation process, and a hydrolysis process. In this case, the substrate sheet 81 is removed from the laminated body 10K after the impregnation process, the electrolyte of the laminated body 10K is given an ion exchange function after the hydrolysis process, and a membrane electrode including the composite electrolyte membrane 100E can be obtained Assembly 50B.

这样,与第二实施例类似,可抑制阳极催化剂层13a和阴极催化剂层13b的移位,可防止燃料电池的单元电池的组装不良,并且可抑制发电期间燃料电池性能的分散。在以上述方式制造的复合型电解质膜100E中,保水材料被固定在电解质膜100E的厚度方向上的中心。结果,可防止保水材料14在水移动的作用下移动,并且可抑制燃料电池发电期间的流动损失。结果,可确保稳定的质子传导性。In this way, similar to the second embodiment, displacement of the anode catalyst layer 13a and the cathode catalyst layer 13b can be suppressed, poor assembly of unit cells of the fuel cell can be prevented, and dispersion of fuel cell performance during power generation can be suppressed. In the composite type electrolyte membrane 100E manufactured in the above manner, the water retaining material is fixed at the center in the thickness direction of the electrolyte membrane 100E. As a result, the water retaining material 14 can be prevented from moving due to water movement, and flow loss during fuel cell power generation can be suppressed. As a result, stable proton conductivity can be ensured.

图8示出按照本发明的用于制造复合型电解质膜的方法的第六实施例。第六实施例的制造方法与第四实施例的不同之处在于,在层叠工序之前配置保水材料。第六实施例的制造方法包括上述的浸渍工序、折叠工序和水解工序,这些工序采用相同的附图标记并省略其详细说明。FIG. 8 shows a sixth embodiment of the method for manufacturing a composite electrolyte membrane according to the present invention. The manufacturing method of the sixth embodiment differs from the fourth embodiment in that a water-retaining material is placed before the lamination process. The manufacturing method of the sixth embodiment includes the above-mentioned dipping process, folding process, and hydrolysis process, and these processes use the same reference numerals and their detailed descriptions are omitted.

如图8所示,在层叠工序中,首先,配置保水材料14。配置方法与上述实施例相同。然后,在层叠工序中,将电解质板片11和加强板片12配置成使得保水材料14配置在电解质板片11和加强板片12之间。由于接合是通过使电解质板片11的电解质从加强板片12的一侧浸渍而进行的,所以在接合之后在层叠体10P中在电解质层11a和加强层12a之间形成其中保水材料14作为添加剂被添加到电解质的添加层14b。然后,通过折叠工序、浸渍工序和水解工序获得复合型电解质膜100F。As shown in FIG. 8 , in the lamination process, first, the water-retaining material 14 is arranged. The configuration method is the same as the above embodiment. Then, in the lamination process, the electrolyte sheet 11 and the reinforcement sheet 12 are arranged such that the water retaining material 14 is arranged between the electrolyte sheet 11 and the reinforcement sheet 12 . Since the bonding is performed by impregnating the electrolyte of the electrolyte sheet 11 from one side of the reinforcing sheet 12, a water-retaining material 14 is formed between the electrolyte layer 11a and the reinforcing layer 12a in the laminated body 10P after bonding. The additive layer 14b is added to the electrolyte. Then, the composite electrolyte membrane 100F is obtained through a folding process, an impregnation process, and a hydrolysis process.

这样,如图8所示,可获得复合型电解质膜100F,其至少包括作为电解质层的第一电解层11a、其中保水材料作为添加剂被添加到电解质并将第一电解质层11a夹在中间的添加层14b、形成为将添加层14b夹在中间并浸渍有电解质的加强层12b和形成在加强层12b的表面上的第二电解质层11b,前述层沿膜的厚度方向堆叠。In this way, as shown in FIG. 8, a composite electrolyte membrane 100F can be obtained, which includes at least a first electrolytic layer 11a as an electrolyte layer, wherein a water-retaining material is added to the electrolyte as an additive and sandwiches the first electrolyte layer 11a. Layer 14b, reinforcement layer 12b formed to sandwich additive layer 14b and impregnated with electrolyte, and second electrolyte layer 11b formed on the surface of reinforcement layer 12b are stacked in the thickness direction of the membrane.

在以上述方式获得的复合型电解质膜100F中,层叠体10A被折叠成使得电解质层11a的表面的一部分位于另一部分上,并且加强层12a变成电解质膜的表面。因此,电解质层11a形成在复合型电解质膜100F的厚度方向上的中心,浸渍有电解质的加强层12b配置在靠近电解质膜的厚度方向上的表面的表面层部分中,并且添加层可配置在其附近。结果,不仅可改善燃料电池工作过程中电解质膜100F的蠕变性能,而且可进一步改善电解质膜100F的保水能力。In composite electrolyte membrane 100F obtained in the above manner, laminated body 10A is folded such that one part of the surface of electrolyte layer 11a lies on the other, and reinforcement layer 12a becomes the surface of the electrolyte membrane. Therefore, the electrolyte layer 11a is formed at the center in the thickness direction of the composite type electrolyte membrane 100F, the reinforcement layer 12b impregnated with electrolyte is arranged in the surface layer portion close to the surface in the thickness direction of the electrolyte membrane, and the additional layer may be arranged thereon. nearby. As a result, not only the creep performance of the electrolyte membrane 100F during operation of the fuel cell can be improved, but also the water retention capacity of the electrolyte membrane 100F can be further improved.

图9是示出本发明一个实施例的用于制造膜电极组件的方法的示意图,该图用于说明应用于图9所示的膜电极组件的第二折叠工序。如图9所示,准备由带状电解质构成的板片(电解质板片)11和由为多孔聚合物材料的聚四氟乙烯(PTFE)构成的带状加强板片12。然后,在层叠工序中,对电解质板片11和加强板片12进行加热、加压和层叠,并制造出层叠体10A,其中电解质板片用作电解质层11a,而加强板片12用作加强层12a。FIG. 9 is a schematic view showing a method for manufacturing a membrane electrode assembly according to an embodiment of the present invention, which is used to explain a second folding process applied to the membrane electrode assembly shown in FIG. 9 . As shown in FIG. 9 , a sheet (electrolyte sheet) 11 made of a belt-shaped electrolyte and a belt-shaped reinforcing sheet 12 made of polytetrafluoroethylene (PTFE), which is a porous polymer material, are prepared. Then, in the lamination process, the electrolyte sheet 11 and the reinforcing sheet 12 are heated, pressurized, and laminated, and a laminated body 10A is manufactured in which the electrolyte sheet is used as the electrolyte layer 11a and the reinforcing sheet 12 is used as the reinforcing sheet. Layer 12a.

然后,在层叠体10A已形成后将阳极催化剂层13a和阴极催化剂层13b配置在电解质层11a的表面上,并制造出具有形成在其上的催化剂层13a、13b的层叠体10D。Then, anode catalyst layer 13a and cathode catalyst layer 13b are disposed on the surface of electrolyte layer 11a after laminate 10A has been formed, and laminate 10D having catalyst layers 13a, 13b formed thereon is produced.

更具体地,在催化剂配置工序中,在层叠体10A已形成后在电解质层11a的表面上沿层叠体10A的横向方向S形成两排阳极催化剂层13a和阴极催化剂层13b。此外,阳极催化剂层13a和阴极催化剂层13b还沿纵向方向(传送方向)L配置成使得多个阳极催化剂层13a和多个阴极催化剂层13b交替形成(换句话说,使得两排阳极催化剂层13a和阴极催化剂层13b对角地形成),并且通过加压及在等于或低于170℃的温度下加热来固定这些层。More specifically, in the catalyst disposition process, two rows of anode catalyst layer 13a and cathode catalyst layer 13b are formed on the surface of electrolyte layer 11a in the lateral direction S of laminate 10A after laminate 10A has been formed. In addition, the anode catalyst layers 13a and the cathode catalyst layers 13b are also arranged in the longitudinal direction (conveying direction) L such that a plurality of anode catalyst layers 13a and a plurality of cathode catalyst layers 13b are alternately formed (in other words, two rows of anode catalyst layers 13a formed diagonally to the cathode catalyst layer 13b), and these layers were fixed by applying pressure and heating at a temperature equal to or lower than 170°C.

以与第二实施例中相同的方式,对催化剂层13a、13b的配置可通过利用喷射器吹送、通过采用底衬板片、或通过利用工具或涂覆模转移来进行,并且配置方法不受特别限制,只要多个催化剂层13a、13b能以上述布置配置在电解质层11a的期望表面上即可。In the same manner as in the second embodiment, the configuration of the catalyst layers 13a, 13b can be performed by blowing with an injector, by using a backing sheet, or by transferring using a tool or a coating die, and the configuration method is not affected by It is particularly limited as long as the plurality of catalyst layers 13a, 13b can be arranged on the desired surface of the electrolyte layer 11a in the above arrangement.

然后,在折叠工序中,以与上述几个实施例中相同的方式在层叠体10D的中央部沿纵向方向L折叠层叠体10D,使得阳极催化剂层13a配置在层叠体10E的一个表面上,而阴极催化剂层13b配置在层叠体10E的另一个表面上(阳极催化剂层13a和阴极催化剂层13b配置成将层叠体10E(复合型电解质膜)夹在中间)。然后,在浸渍工序中,使电解质浸渍到加强层12a中,并制造出层叠体10F。在水解工序中,赋予层叠体10F的电解质以离子交换功能,并且可获得包括复合型电解质膜100B的膜电极组件50C。Then, in the folding process, the laminated body 10D is folded in the longitudinal direction L at the central portion of the laminated body 10D in the same manner as in the above-described several embodiments so that the anode catalyst layer 13a is arranged on one surface of the laminated body 10E, and The cathode catalyst layer 13b is arranged on the other surface of the laminate 10E (the anode catalyst layer 13a and the cathode catalyst layer 13b are arranged to sandwich the laminate 10E (composite electrolyte membrane) therebetween). Then, in the impregnation step, the electrolyte is impregnated into the reinforcement layer 12 a to manufacture the laminated body 10F. In the hydrolysis process, an ion exchange function is imparted to the electrolyte of the laminate 10F, and a membrane electrode assembly 50C including the composite electrolyte membrane 100B can be obtained.

由于阳极催化剂层13a和阴极催化剂层13b沿横向方向S形成在同一表面(在该表面中在层叠工序后已形成层叠体的电解质层11a)内,所以这些催化剂层13a、13b可无移位地精确配置以将复合型电解质膜100B夹在中间。结果,在保持折叠工序中层叠体10E的折叠位置精度的情况下,可抑制阳极催化剂层13a和阴极催化剂层13b的相互布置的移位,可防止在燃料电池1的下述组装中产生组装不良,并且可抑制在燃料电池1发电期间的性能分散。Since the anode catalyst layer 13a and the cathode catalyst layer 13b are formed in the same surface (in which the electrolyte layer 11a of the laminate has been formed after the lamination process) in the lateral direction S, these catalyst layers 13a, 13b can be separated without displacement. Precisely configured to sandwich the composite electrolyte membrane 100B. As a result, the displacement of the mutual arrangement of the anode catalyst layer 13 a and the cathode catalyst layer 13 b can be suppressed while maintaining the accuracy of the folding position of the stacked body 10E in the folding process, and it is possible to prevent assembly defects in the following assembly of the fuel cell 1 . , and performance dispersion during power generation by the fuel cell 1 can be suppressed.

膜电极组件50C是带状膜电极组件,并且由于多个阳极催化剂层13a和多个阴极催化剂层13b沿纵向方向在膜电极组件50C的表面上交替形成,所以可通过下述的第二折叠工序容易地制造燃料电池。The membrane electrode assembly 50C is a belt-shaped membrane electrode assembly, and since a plurality of anode catalyst layers 13a and a plurality of cathode catalyst layers 13b are alternately formed on the surface of the membrane electrode assembly 50C in the longitudinal direction, it is possible to pass through the second folding process described below. Fuel cells are easily fabricated.

于是,对膜电极组件50C进行第二折叠。更具体地,如图10所示,在水解工序后进行的第二折叠工序中,沿横向方向S(沿图中的C1-C1、C2-C2、...)折叠膜电极组件50C,使得阳极催化剂层13a与在纵向方向L上邻接阳极催化剂层13a的阴极催化剂层13b彼此面对。Then, the second folding is performed on the membrane electrode assembly 50C. More specifically, as shown in FIG. 10 , in the second folding process performed after the hydrolysis process, the membrane electrode assembly 50C is folded in the lateral direction S (along C1-C1, C2-C2, ... in the figure), such that The anode catalyst layer 13a and the cathode catalyst layer 13b adjacent to the anode catalyst layer 13a in the longitudinal direction L face each other.

这种折叠可例如通过准备具有使得下述隔板能够导入的厚度的折叠工具、沿横向方向S挤压折叠工具的末端、并且折叠而来进行,但是折叠方法不受特别限制,只要折叠可进行为使得在纵向方向L上邻接的催化剂层13a、13b彼此面对即可。Such folding can be performed, for example, by preparing a folding tool having a thickness such that a separator described below can be introduced, pressing the tip of the folding tool in the transverse direction S, and folding, but the folding method is not particularly limited as long as the folding can be performed The catalyst layers 13 a , 13 b adjacent in the longitudinal direction L may face each other.

在第二折叠工序以上述方式进行的情况下,如果下述的隔板等配置在这些相对的催化剂层13a、13b之间,则可从一个连续的膜电极组件50C容易地制造出其中无移位地形成催化剂层13a、13b的燃料电池的单个电池,而无需使多个膜电极组件层叠。In the case where the second folding process is carried out in the above-mentioned manner, if the following separators and the like are arranged between these opposing catalyst layers 13a, 13b, it is possible to easily manufacture from one continuous membrane electrode assembly 50C without displacement. A single cell of the fuel cell in which the catalyst layers 13a, 13b are formed in place without stacking a plurality of membrane electrode assemblies.

此外,由于多个阳极催化剂层13a和多个阴极催化剂层13b沿纵向方向L交替形成,并且阴极催化剂层13b总是形成于在纵向方向L上邻接阳极催化剂层13a的层中,所以第二折叠工序形成多个具有同一方向的表面(与扩散层15接触的表面)的阳极催化剂层13a,并形成多个具有与前述方向相反的同一方向的表面(与扩散层15接触的表面)的阴极催化剂层13b。结果,可防止在以通常的方法层叠多个膜电极组件时可能产生的膜电极组件的阳极催化剂层和阴极催化剂层的组装误差。Furthermore, since a plurality of anode catalyst layers 13a and a plurality of cathode catalyst layers 13b are alternately formed in the longitudinal direction L, and the cathode catalyst layers 13b are always formed in a layer adjacent to the anode catalyst layer 13a in the longitudinal direction L, the second fold The process forms a plurality of anode catalyst layers 13a having a surface in the same direction (a surface in contact with the diffusion layer 15), and forms a plurality of cathode catalyst layers having a surface in the same direction opposite to the aforementioned direction (a surface in contact with the diffusion layer 15). Layer 13b. As a result, an assembly error of the anode catalyst layer and the cathode catalyst layer of the membrane electrode assembly, which may occur when a plurality of membrane electrode assemblies are stacked in a usual method, can be prevented.

下面将描述一种利用以上述方式制造的膜电极组件制造燃料电池的方法。图11示出用于从图10所示的膜电极组件50C制造燃料电池的方法。A method of manufacturing a fuel cell using the membrane electrode assembly manufactured in the above manner will be described below. FIG. 11 shows a method for manufacturing a fuel cell from the membrane electrode assembly 50C shown in FIG. 10 .

在本实施例中,用于制造燃料电池的方法包括在第二折叠工序后在膜电极组件50C的阳极催化剂层13a和阴极催化剂层13b的表面上配置扩散层15、然后在具有彼此相对配置的扩散层的阳极催化剂层13a和阴极催化剂层13b之间配置隔板60的工序,所述隔板60中形成有燃料气体流路61和氧气流路62。In this embodiment, the method for manufacturing a fuel cell includes disposing the diffusion layer 15 on the surfaces of the anode catalyst layer 13a and the cathode catalyst layer 13b of the membrane electrode assembly 50C after the second folding process, and then disposing the A step of disposing the separator 60 in which the fuel gas flow path 61 and the oxygen flow path 62 are formed between the anode catalyst layer 13 a and the cathode catalyst layer 13 b of the diffusion layer.

更具体地,准备在其中形成有燃料气体流路61和氧气流路62的隔板60。然后,在隔板60的两个表面上配置用于配置在阳极催化剂层13a和阴极催化剂层13b的表面上的扩散层15。然后,将能够密封膜电极组件50C并粘附于其上的构件63附接到隔板60的纵向方向上的两端。More specifically, the separator 60 in which the fuel gas flow path 61 and the oxygen flow path 62 are formed is prepared. Then, the diffusion layer 15 for being arranged on the surfaces of the anode catalyst layer 13 a and the cathode catalyst layer 13 b is arranged on both surfaces of the separator 60 . Then, members 63 capable of sealing and adhering the membrane electrode assembly 50C are attached to both ends of the separator 60 in the longitudinal direction.

将具有扩散层15和附接有密封剂63的隔板60朝膜电极组件50C的折叠部分插入,使得扩散层15位于膜电极组件50C的阳极催化剂层13a和阴极催化剂层13b上。结果,通过将扩散层15和隔板60夹在膜电极组件50C的相对的催化剂层13a、13b的上表面上而形成层叠的电极,并且后续的加热和沿厚度方向的加压制造出其中堆叠有多个单元电池的燃料电池1。Separator 60 with diffusion layer 15 and sealant 63 attached is inserted toward the folded portion of MEA 50C such that diffusion layer 15 is located on anode catalyst layer 13 a and cathode catalyst layer 13 b of MEA 50C. As a result, a laminated electrode is formed by sandwiching the diffusion layer 15 and the separator 60 on the upper surfaces of the opposing catalyst layers 13a, 13b of the membrane electrode assembly 50C, and subsequent heating and pressure in the thickness direction produce a stacked A fuel cell 1 having a plurality of unit cells.

通过上述方法,与在多个膜电极组件之间配置隔板的通常的方法相比,可减少操作工步的数量,并且由于可在第二折叠工序后以连续的方式配置隔板,所以可抑制在形成燃料电池1的单元电池的过程中混入污染物。By the above method, compared with the usual method of arranging separators between a plurality of membrane electrode assemblies, the number of operation steps can be reduced, and since separators can be arranged in a continuous manner after the second folding process, it is possible to Incorporation of pollutants in the process of forming the unit cells of the fuel cell 1 is suppressed.

图12示出用于从由图11所示的制造方法制造的燃料电池制造包括期望数量的单元电池的燃料电池的方法。如图12所示,在由图11所示的制造方法制造的燃料电池1中,由多个单元电池构成的燃料电池在绝缘状态下通过电解质膜连接。因此,如图11所示,可通过切断连接部分的电解质膜而在组合状态(从几个单元电池到几百个单元电池)下获得由必需数量的单元电池构成的燃料电池1A、1b,而没有在电池层叠期间产生的在取向(阳极/阴极表面的取向)的相互布置方面的组装误差。FIG. 12 shows a method for manufacturing a fuel cell including a desired number of unit cells from the fuel cell manufactured by the manufacturing method shown in FIG. 11 . As shown in FIG. 12, in the fuel cell 1 manufactured by the manufacturing method shown in FIG. 11, the fuel cell composed of a plurality of unit cells is connected through an electrolyte membrane in an insulated state. Therefore, as shown in FIG. 11, a fuel cell 1A, 1b composed of a necessary number of unit cells can be obtained in an assembled state (from several unit cells to hundreds of unit cells) by cutting off the electrolyte membrane at the connecting portion, while There are no assembly errors in the mutual arrangement of the orientation (orientation of the anode/cathode surfaces) that occur during cell stacking.

在上文中描述了按照本发明的复合型电解质膜、膜电极组件和燃料电池的实施例及用于制造它们的方法,但是,本发明不限于这些实施例,而是可在不背离在所附权利要求中描述的本发明的实质的情况下作出各种设计变型。The embodiments of the composite electrolyte membrane, the membrane electrode assembly and the fuel cell according to the present invention and the method for manufacturing them are described above, however, the present invention is not limited to these embodiments, but can be used without departing from the appended Various design modifications are made without compromising the essence of the present invention described in the claims.

例如,在第四至第六实施例中,使用保水材料作为添加剂,但是也可使用由过渡金属如铈的氧化物构成的自由基抑制剂,以将在燃料电池发电期间作为副产物产生的过氧化氢分解成水和氧并抑制羟自由基的产生。For example, in the fourth to sixth embodiments, a water-retaining material is used as an additive, but a radical inhibitor composed of an oxide of a transition metal such as cerium may also be used to suppress superfluous particles generated as a by-product during power generation of a fuel cell. Hydrogen oxide decomposes into water and oxygen and inhibits the generation of hydroxyl radicals.

此外,在第一至第六实施例中制造的复合型电解质膜中,用作在折叠工序中形成的折叠余量的折叠端部可用切割器等切除。Furthermore, in the composite type electrolyte membranes produced in the first to sixth embodiments, the folded ends serving as the folding margin formed in the folding process can be cut off with a cutter or the like.

在第二至第五实施例中,催化剂层被附加地配置,但是显然,可通过在催化剂层附加地配置图14所示的扩散层和隔板来获得燃料电池。In the second to fifth embodiments, the catalyst layer is additionally arranged, but obviously, a fuel cell can be obtained by additionally arranging the diffusion layer and the separator shown in FIG. 14 on the catalyst layer.

此外,在图11所示的实施例中,在配置扩散层和隔板时,具有形成在其表面上的扩散层的隔板通过插入到膜电极组件的折叠部分中而配置在膜电极组件中,但是该方法不受限制,扩散层和隔板也可分开配置,只要扩散层和隔板可配置在膜电极组件中并且可制造出燃料电池即可。此外,在本实施例中,在层叠工序后配置催化剂层,但是阳极催化剂层和阴极催化剂层也可进一步配置于配置在隔板上的扩散层上,而无需将催化剂层配置在电解质膜上,只要可精确地配置阳极催化剂层和阴极催化剂层即可。In addition, in the embodiment shown in FIG. 11, when arranging the diffusion layer and the separator, the separator having the diffusion layer formed on its surface is arranged in the membrane electrode assembly by being inserted into the folded portion of the membrane electrode assembly. , but the method is not limited, and the diffusion layer and the separator can also be arranged separately, as long as the diffusion layer and the separator can be arranged in the membrane electrode assembly and a fuel cell can be manufactured. In addition, in this embodiment, the catalyst layer is disposed after the stacking process, but the anode catalyst layer and the cathode catalyst layer may be further disposed on the diffusion layer disposed on the separator without disposing the catalyst layer on the electrolyte membrane, It is only necessary that the anode catalyst layer and the cathode catalyst layer can be precisely arranged.

此外,在图9至12所示的实施例中,例如为保水剂和自由基抑制剂的添加剂未配置在复合型电解质膜中,但是对于在图5、7和8所示的第四至第六实施例中描述的方法,例如为保水剂和自由基抑制剂的添加剂可配置在复合型电解质膜中。In addition, in the embodiments shown in FIGS. 9 to 12, additives such as water retention agents and free radical inhibitors are not configured in the composite electrolyte membrane, but for the fourth to fourth shown in FIGS. 5, 7 and 8 In the method described in the sixth embodiment, additives such as water retaining agent and free radical inhibitor can be configured in the composite electrolyte membrane.

尽管已参照本发明的示例性实施例描述了本发明,但是应当理解,本发明不限于所述示例性实施例或构型。相反,本发明意图涵盖各种变型和等同布置。此外,虽然以作为示例的各种组合和构型示出了示例性实施例的各种要素,但是包括更多、更少或仅单个要素的其它组合和构型也在本发明的精神和范围内。While the invention has been described with reference to exemplary embodiments thereof, it is to be understood that the invention is not limited to the exemplary embodiments or configurations. On the contrary, the invention is intended to cover various modifications and equivalent arrangements. In addition, while the various elements of the exemplary embodiments are shown in various combinations and configurations that are illustrative, other combinations and configurations, including more, less or only a single element, are also within the spirit and scope of the invention. Inside.

Claims (12)

1.一种用于制造膜电极组件的方法,包括用于制造复合型电解质膜的方法,所述用于制造复合型电解质膜的方法包括:1. A method for manufacturing a membrane electrode assembly, comprising a method for manufacturing a composite electrolyte membrane, the method for manufacturing a composite electrolyte membrane comprising: 通过使作为电解质层(11a)的包括电解质的电解质板片(11)与作为加强层(12a)的包括多孔聚合物材料的加强板片(12)层叠和一体化而获得层叠体的层叠工序;A lamination process for obtaining a laminated body by laminating and integrating an electrolyte sheet (11) comprising an electrolyte as an electrolyte layer (11a) and a reinforcing sheet (12) comprising a porous polymer material as a reinforcing layer (12a); 将由所述层叠工序获得的所述层叠体折叠成使得所述层叠体的表面的一部分位于该表面的另一部分上的第一折叠工序;a first folding process of folding said laminate obtained by said laminating process such that a part of a surface of said laminate is located on another part of the surface; 使被折叠的所述层叠体的所述电解质浸渍到所述加强层(12a)中的浸渍工序;和an impregnation process of impregnating the electrolyte of the folded laminated body into the reinforcing layer (12a); and 使所述层叠体中浸渍的所述电解质水解的水解工序;a hydrolysis step of hydrolyzing the electrolyte impregnated in the laminate; 其中in 在所述第一折叠工序中,将所述层叠体折叠成使得所述层叠体中在所述加强层(12a)侧的表面的一部分位于该表面的另一部分上;In the first folding process, folding the laminated body such that a part of the surface of the laminated body on the reinforcing layer (12a) side is positioned on another part of the surface; 在所述层叠工序中,形成带状层叠体,并且在所述层叠体已形成后,在所述电解质层(11a)的表面上配置阳极催化剂层(13a)和阴极催化剂层(13b),使得所述阳极催化剂层(13a)和所述阴极催化剂层(13b)沿所述层叠体的横向方向形成;In the lamination step, a belt-shaped laminate is formed, and after the laminate has been formed, an anode catalyst layer (13a) and a cathode catalyst layer (13b) are disposed on the surface of the electrolyte layer (11a) such that The anode catalyst layer (13a) and the cathode catalyst layer (13b) are formed along the lateral direction of the stack; 在所述第一折叠工序中,将所述层叠体沿纵向方向折叠成使得所述阳极催化剂层(13a)配置在所述层叠体的一个表面上,而所述阴极催化剂层(13b)配置在所述层叠体的另一个表面上;In the first folding process, the laminate is folded in the longitudinal direction so that the anode catalyst layer (13a) is arranged on one surface of the laminate, and the cathode catalyst layer (13b) is arranged on on the other surface of the laminate; 在所述层叠工序中,将所述阳极催化剂层(13a)和所述阴极催化剂层(13b)配置成使得多个所述阳极催化剂层(13a)和多个所述阴极催化剂层(13b)沿所述纵向方向交替形成;以及In the stacking step, the anode catalyst layer (13a) and the cathode catalyst layer (13b) are arranged such that a plurality of the anode catalyst layers (13a) and a plurality of the cathode catalyst layers (13b) are along said longitudinal directions alternate; and 所述用于制造膜电极组件的方法还包括在所述水解工序后将所述层叠体沿所述横向方向折叠成使得所述阳极催化剂层(13a)与在所述纵向方向上邻接所述阳极催化剂层(13a)的所述阴极催化剂层(13b)彼此面对的第二折叠工序。The method for manufacturing a membrane electrode assembly further includes folding the stacked body in the transverse direction after the hydrolysis process so that the anode catalyst layer (13a) is adjacent to the anode in the longitudinal direction. The second folding process of said cathode catalyst layers (13b) of catalyst layers (13a) facing each other. 2.根据权利要求1所述的用于制造膜电极组件的方法,其中,在所述层叠工序中,通过加热和层叠所述电解质板片(11)与所述加强板片(12)来形成所述层叠体。2. The method for manufacturing a membrane electrode assembly according to claim 1, wherein, in the lamination process, formed by heating and laminating the electrolyte sheet (11) and the reinforcing sheet (12) the laminate. 3.根据权利要求1所述的用于制造膜电极组件的方法,其中,在所述浸渍工序中,加热被折叠的所述层叠体直到所述电解质溶解,并且使所述电解质浸渍到所述加强层(12a)中。3. The method for manufacturing a membrane electrode assembly according to claim 1, wherein, in the impregnation process, the folded laminate is heated until the electrolyte is dissolved, and the electrolyte is impregnated into the In the reinforcement layer (12a). 4.根据权利要求2所述的用于制造膜电极组件的方法,其中,在所述浸渍工序中,加热被折叠的所述层叠体直到所述电解质溶解,并且使所述电解质浸渍到所述加强层(12a)中。4. The method for manufacturing a membrane electrode assembly according to claim 2, wherein, in the impregnation process, the folded laminate is heated until the electrolyte is dissolved, and the electrolyte is impregnated into the In the reinforcement layer (12a). 5.根据权利要求1所述的用于制造膜电极组件的方法,其中,在所述层叠工序中,在所述层叠体已形成后,在所述加强层(12a)的表面上配置将过氧化氢分解成水和氧并抑制羟自由基产生的自由基抑制剂与保水材料(14)中的至少一者。5. The method for manufacturing a membrane electrode assembly according to claim 1, wherein, in the stacking process, after the stacked body has been formed, an overcoat is disposed on the surface of the reinforcing layer (12a). At least one of a free radical inhibitor that decomposes hydrogen oxide into water and oxygen and suppresses generation of hydroxyl radicals, and a water-retaining material (14). 6.根据权利要求1至4中任一项所述的用于制造膜电极组件的方法,其中,在所述层叠工序中,在所述电解质板片(11)和所述加强板片(12)之间配置将过氧化氢分解成水和氧并抑制羟自由基产生的自由基抑制剂与保水材料(14)中的至少一者。6. The method for manufacturing a membrane electrode assembly according to any one of claims 1 to 4, wherein, in the lamination process, the electrolyte sheet (11) and the reinforcing sheet (12 ) and at least one of a free radical inhibitor and a water-retaining material (14) that decomposes hydrogen peroxide into water and oxygen and inhibits the generation of hydroxyl radicals is arranged. 7.一种用于制造燃料电池的方法,包括根据权利要求1所述的用于制造膜电极组件的方法,其特征在于还包括扩散层和隔板配置工序,所述扩散层和隔板配置工序在所述第二折叠工序后在所述膜电极组件的所述阳极催化剂层(13a)的表面和所述阴极催化剂层(13b)的表面上配置扩散层(15),以及在具有彼此相对配置的所述扩散层(15)的所述阳极催化剂层(13a)和所述阴极催化剂层(13b)之间配置隔板(60),所述隔板(60)中形成有燃料气体流路(61)和氧气流路(62),使得所述燃料气体流路(61)位于所述阳极催化剂层(13a)侧,而所述氧气流路(62)位于所述阴极催化剂层(13b)侧。7. A method for manufacturing a fuel cell, comprising the method for manufacturing a membrane electrode assembly according to claim 1, characterized in that it also includes a diffusion layer and separator configuration process, the diffusion layer and separator configuration process After the second folding process, disposing a diffusion layer (15) on the surface of the anode catalyst layer (13a) and the surface of the cathode catalyst layer (13b) of the membrane electrode assembly, and A separator (60) is arranged between the anode catalyst layer (13a) and the cathode catalyst layer (13b) of the configured diffusion layer (15), and a fuel gas flow path is formed in the separator (60). (61) and an oxygen flow path (62), so that the fuel gas flow path (61) is located on the anode catalyst layer (13a) side, and the oxygen flow path (62) is located on the cathode catalyst layer (13b) side. 8.一种膜电极组件,至少包括一对阳极催化剂层(13a)和阴极催化剂层(13b),所述阳极催化剂层和阴极催化剂层配置在复合型电解质膜的两个表面上,以便将所述复合型电解质膜夹在中间,所述复合型电解质膜至少具有电解质层(11a)和加强层(12a),所述电解质层包括电解质,在所述加强层中多孔聚合物材料浸渍有所述电解质,8. A membrane electrode assembly, comprising at least a pair of anode catalyst layer (13a) and cathode catalyst layer (13b), said anode catalyst layer and cathode catalyst layer are configured on both surfaces of the composite electrolyte membrane, so that the The composite electrolyte membrane is sandwiched in the middle, and the composite electrolyte membrane has at least an electrolyte layer (11a) and a reinforcement layer (12a), the electrolyte layer includes electrolyte, and the porous polymer material is impregnated with the electrolyte, 所述膜电极组件的特征在于The membrane electrode assembly is characterized in that 所述复合型电解质膜包括:The composite electrolyte membrane includes: 添加层(14b),在所述添加层中,将过氧化氢分解成水和氧并抑制羟自由基产生的自由基抑制剂与保水材料(14)中的至少一者被添加到所述电解质;An added layer (14b) in which at least one of a radical inhibitor that decomposes hydrogen peroxide into water and oxygen and suppresses generation of hydroxyl radicals and a water-retaining material (14) is added to the electrolyte ; 形成为将所述添加层(14b)夹在中间的所述加强层(12a);和said reinforcing layer (12a) formed to sandwich said added layer (14b); and 形成在每个所述加强层(12a)的表面上的所述电解质层(11a);并且其中:said electrolyte layer (11a) formed on the surface of each said reinforcement layer (12a); and wherein: 所述膜电极组件是带状膜电极组件,并且所述阳极催化剂层(13a)和所述阴极催化剂层(13b)在所述膜电极组件的表面上沿纵向方向交替形成,以及the membrane electrode assembly is a strip-shaped membrane electrode assembly, and the anode catalyst layers (13a) and the cathode catalyst layers (13b) are alternately formed on the surface of the membrane electrode assembly in the longitudinal direction, and 其中所述膜电极组件沿横向方向折叠成使得所述阳极催化剂层(13a)与在所述纵向方向上邻接所述阳极催化剂层(13a)的所述阴极催化剂层(13b)彼此面对。Wherein the membrane electrode assembly is folded in the transverse direction such that the anode catalyst layer (13a) and the cathode catalyst layer (13b) adjacent to the anode catalyst layer (13a) in the longitudinal direction face each other. 9.一种包括根据权利要求8所述的膜电极组件的燃料电池,其特征在于包括:9. A fuel cell comprising the membrane electrode assembly according to claim 8, characterized in that it comprises: 所述膜电极组件;the membrane electrode assembly; 扩散层(15),所述扩散层配置在所述膜电极组件的所述阳极催化剂层(13a)的表面和所述阴极催化剂层(13b)的表面上;和a diffusion layer (15) disposed on the surface of the anode catalyst layer (13a) and the surface of the cathode catalyst layer (13b) of the membrane electrode assembly; and 隔板(60),所述隔板(60)中至少形成有位于所述阳极催化剂层(13a)侧的燃料气体流路(61)和位于所述阴极催化剂层(13b)侧的氧气流路(62),并且所述隔板(60)配置在具有彼此相对配置的所述扩散层(15)的所述阳极催化剂层(13a)和所述阴极催化剂层(13b)之间。A separator (60) in which at least a fuel gas flow path (61) on the side of the anode catalyst layer (13a) and an oxygen flow path on the side of the cathode catalyst layer (13b) are formed (62), and the separator (60) is disposed between the anode catalyst layer (13a) and the cathode catalyst layer (13b) having the diffusion layer (15) disposed opposite to each other. 10.一种膜电极组件,至少包括一对阳极催化剂层(13a)和阴极催化剂层(13b),所述阳极催化剂层和阴极催化剂层配置在复合型电解质膜的两个表面上,以便将所述复合型电解质膜夹在中间,所述复合型电解质膜至少具有电解质层和加强层(12a,12b),所述电解质层包括电解质,在所述加强层中多孔聚合物材料浸渍有所述电解质,10. A membrane electrode assembly, comprising at least a pair of anode catalyst layer (13a) and cathode catalyst layer (13b), said anode catalyst layer and cathode catalyst layer are configured on both surfaces of the composite electrolyte membrane, so that the The composite electrolyte membrane is sandwiched in the middle, the composite electrolyte membrane has at least an electrolyte layer and a reinforcement layer (12a, 12b), the electrolyte layer includes an electrolyte, and the porous polymer material is impregnated with the electrolyte in the reinforcement layer , 所述膜电极组件的特征在于The membrane electrode assembly is characterized in that 所述复合型电解质膜包括:The composite electrolyte membrane includes: 作为所述电解质层的第一电解质层(11a);A first electrolyte layer (11a) as said electrolyte layer; 形成为将所述第一电解质层(11a)夹在中间的添加层(14b),在所述添加层中,将过氧化氢分解成水和氧并抑制羟自由基产生的自由基抑制剂与保水材料(14)中的至少一者被添加到所述电解质;Formed as an additive layer (14b) sandwiching the first electrolyte layer (11a), in the additive layer, a radical inhibitor that decomposes hydrogen peroxide into water and oxygen and suppresses generation of hydroxyl radicals and at least one of water-retaining materials (14) is added to the electrolyte; 形成在所述添加层(14b)的表面上的所述加强层(12a,12b);和said reinforcing layer (12a, 12b) formed on the surface of said added layer (14b); and 用作所述电解质层并形成在所述加强层(12a,12b)的表面上的第二电解质层(11b);并且其中:a second electrolyte layer (11b) serving as said electrolyte layer and formed on the surface of said reinforcement layer (12a, 12b); and wherein: 所述膜电极组件是带状膜电极组件,并且所述阳极催化剂层(13a)和所述阴极催化剂层(13b)在所述膜电极组件的表面上沿纵向方向交替形成,以及the membrane electrode assembly is a strip-shaped membrane electrode assembly, and the anode catalyst layers (13a) and the cathode catalyst layers (13b) are alternately formed on the surface of the membrane electrode assembly in the longitudinal direction, and 其中所述膜电极组件沿横向方向折叠成使得所述阳极催化剂层(13a)与在所述纵向方向上邻接所述阳极催化剂层(13a)的所述阴极催化剂层(13b)彼此面对。Wherein the membrane electrode assembly is folded in the transverse direction such that the anode catalyst layer (13a) and the cathode catalyst layer (13b) adjacent to the anode catalyst layer (13a) in the longitudinal direction face each other. 11.一种包括根据权利要求10所述的膜电极组件的燃料电池,其特征在于包括:11. A fuel cell comprising the membrane electrode assembly according to claim 10, characterized in that comprising: 所述膜电极组件;the membrane electrode assembly; 扩散层(15),所述扩散层配置在所述膜电极组件的所述阳极催化剂层(13a)的表面和所述阴极催化剂层(13b)的表面上;和a diffusion layer (15) disposed on the surface of the anode catalyst layer (13a) and the surface of the cathode catalyst layer (13b) of the membrane electrode assembly; and 隔板(60),所述隔板(60)中至少形成有位于所述阳极催化剂层(13a)侧的燃料气体流路(61)和位于所述阴极催化剂层(13b)侧的氧气流路(62),并且所述隔板(60)配置在具有彼此相对配置的所述扩散层(15)的所述阳极催化剂层(13a)和所述阴极催化剂层(13b)之间。A separator (60) in which at least a fuel gas flow path (61) on the side of the anode catalyst layer (13a) and an oxygen flow path on the side of the cathode catalyst layer (13b) are formed (62), and the separator (60) is arranged between the anode catalyst layer (13a) and the cathode catalyst layer (13b) having the diffusion layer (15) arranged opposite to each other. 12.一种膜电极组件,至少具有一对阳极催化剂层(13a)和阴极催化剂层(13b),所述阳极催化剂层和阴极催化剂层配置在复合型电解质膜的两个表面上,以使得所述阳极催化剂层(13a)和所述阴极催化剂层(13b)将所述复合型电解质膜夹在中间,在所述复合型电解质膜中,包括多孔聚合物材料的加强板片(12)浸渍有包括电解质的电解质板片(11),12. A membrane electrode assembly, at least having a pair of anode catalyst layer (13a) and cathode catalyst layer (13b), said anode catalyst layer and cathode catalyst layer are configured on both surfaces of the composite electrolyte membrane, so that the The anode catalyst layer (13a) and the cathode catalyst layer (13b) sandwich the composite electrolyte membrane, and in the composite electrolyte membrane, a reinforcing sheet (12) comprising a porous polymer material is impregnated with an electrolyte sheet (11) comprising electrolyte, 所述膜电极组件的特征在于The membrane electrode assembly is characterized in that 所述膜电极组件是带状膜电极组件,并且所述阳极催化剂层(13a)和所述阴极催化剂层(13b)在所述膜电极组件的表面上沿纵向方向交替形成,以及the membrane electrode assembly is a strip-shaped membrane electrode assembly, and the anode catalyst layers (13a) and the cathode catalyst layers (13b) are alternately formed on the surface of the membrane electrode assembly in the longitudinal direction, and 其中所述膜电极组件沿横向方向折叠成使得所述阳极催化剂层(13a)与在所述纵向方向上邻接所述阳极催化剂层(13a)的所述阴极催化剂层(13b)彼此面对。Wherein the membrane electrode assembly is folded in the transverse direction such that the anode catalyst layer (13a) and the cathode catalyst layer (13b) adjacent to the anode catalyst layer (13a) in the longitudinal direction face each other.
CN2008801178470A 2007-11-26 2008-11-11 Composite electrolyte membrane, membrane-electrode assembly, fuel cell, and methods for manufacturing same Expired - Fee Related CN101874322B (en)

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