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JP4337162B2 - Method for producing electrolyte membrane for polymer electrolyte fuel cell - Google Patents
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JP4337162B2 - Method for producing electrolyte membrane for polymer electrolyte fuel cell - Google Patents

Method for producing electrolyte membrane for polymer electrolyte fuel cell Download PDF

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Publication number
JP4337162B2
JP4337162B2 JP05057999A JP5057999A JP4337162B2 JP 4337162 B2 JP4337162 B2 JP 4337162B2 JP 05057999 A JP05057999 A JP 05057999A JP 5057999 A JP5057999 A JP 5057999A JP 4337162 B2 JP4337162 B2 JP 4337162B2
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Prior art keywords
electrolyte membrane
membrane
cation exchange
exchange membrane
fuel cell
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JP2000251905A (en
Inventor
浩文 飯坂
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Toyota Motor Corp
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Toyota Motor Corp
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    • 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

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Description

【0001】
【発明の属する技術分野】
本発明は、固体高分子型燃料電池用の電解質膜およびその製造方法に関する。
【0002】
【従来の技術】
従来、この種の固体高分子型燃料電池用の電解質膜としては、電解質膜の表面に表面粗化処理を施してなるものが提案されている(特開平5−258756号公報など)。この電解質膜では、表面に施した表面粗化処理により形成される凹凸の凹部に触媒としての金属を堆積させることにより、電解質膜と触媒とガスとの三相界面で生じる電気化学反応の反応場を拡大させて触媒の利用率を高め、電池特性の向上を図ることができるとされている。
【0003】
【発明が解決しようとする課題】
しかしながら、こうした電解質膜では、その凹部に堆積した触媒のうち膜表面付近の触媒粒子が電気化学反応に寄与するだけで、その凹部に堆積した多くの触媒粒子は反応に寄与しないといった問題があった。こうした問題は、触媒として貴金属を用いる場合には、電解質膜を用いる燃料電池のコストを増大させるという問題を併発する。
【0004】
また、表面に粗化処理を施した電解質膜では、処理方法にもよるが膜の表面の構造が化学的に変質されたり、物理的に破壊されるおそれがあり、電解質膜として有効に機能しない部分を生じるという問題もあった。通常、電解質膜としてイオン交換膜を用いるが、化学的な表面処理や物理的な表面処理によりイオン交換に寄与する官能基が破壊される場合があり、この場合、イオン交換の機能を失い、電解質膜としての性能を低下させてしまう。
【0005】
なお、こうした問題の一部を解決するものとして、出願人は、電解質膜表面にプラズマスパッタエッチング処理を施して膜表面に凹凸を形成し、その凹凸に沿ってほぼ一様な厚さの触媒層を形成してなる電解質膜を提案している(特願平6−315502号)。
【0006】
本発明の固体高分子型燃料電池用の電解質膜は、電解質膜としての性能を低下させることなく触媒との接触面積を多くして反応性を高めることを目的とする。本発明の固体高分子型燃料電池用の電解質膜の製造方法は、電解質膜としての性能を低下させることなく触媒との接触面積が多くとれる電解質膜の製造方法を提供することを目的とする。
【0007】
【課題を解決するための手段およびその作用・効果】
本発明の固体高分子型燃料電池用の電解質膜およびその製造方法は、上述の目的の少なくとも一部を達成するために以下の手段を採った。
【0008】
本発明の固体高分子型燃料電池用の電解質膜の製造方法は、
固体高分子型燃料電池に用いられる電解質膜の製造方法であって、
陽イオン交換膜のプロトンを重金属で置換する重金属置換工程と、
該置換された陽イオン交換膜の少なくとも一方の面に放射線を照射して該面に所定形状の窪みを複数形成する表面処理を行なう表面処理工程と、
該表面処理された陽イオン交換膜の前記重金属をプロトンに置換するプロトン置換工程と
を備えることを要旨とする。
【0009】
この本発明の固体高分子型燃料電池用の電解質膜の製造方法では、陽イオン交換膜のプロトンを重金属で置換することにより表面処理の際にイオン交換に寄与する官能基を変質や破壊から防止することができる。この結果、表面処理により電解質膜の性能を低下させることがない。また、表面処理により膜の表面に所定形状の窪みを複数形成するから、触媒との接触面積を多くすることができる。ここで、「放射線」には、プラズマや電子線,X線,γ線などが含まれる。また、「重金属」には、鉛,亜鉛,アルミニウム,鉄,白金などが含まれる。
【0010】
こうした本発明の固体高分子型燃料電池用の電解質膜の製造方法において、前記陽イオン交換膜として強酸性陽イオン交換膜を用いるものとすることもできる。また、本発明の固体高分子型燃料電池用の電解質膜の製造方法において、前記重金属置換工程は、前記重金属の弱酸塩水溶液を用いて置換する工程であるものとすることもできる。ここで、「重金属の弱酸塩水溶液」には、酢酸による重金属塩の水溶液(例えば、酢酸鉛や酢酸亜鉛などの水溶液)などが含まれる。
【0011】
本発明の固体高分子型燃料電池用の電解質膜の製造方法において、前記表面処理工程は、前記放射線として電子線を用いて行なう工程であるものとすることもできる。電子線は制御しやすいから、膜の表面に所定形状の窪みを容易に形成することができる。また、電子線はプラズマやX線,γ線に比して安価に得られるから、電解質膜の製造コストを低減することができる。
【0012】
本発明の第1の固体高分子型燃料電池用の電解質膜は、
固体高分子型燃料電池に用いられる電解質膜であって、
陽イオン交換膜のプロトンを重金属で置換し、該置換された陽イオン交換膜の少なくとも一方の面に放射線を照射して該面に所定の形状の窪みを複数形成し、該所定形状の窪みが複数形成された陽イオン交換膜の前記重金属をプロトンに置換してなる
ことを要旨とする。
【0013】
本発明の第1の固体高分子型燃料電池用の電解質膜では、陽イオン交換膜のプロトンを重金属で置換して表面処理し、表面処理された膜の表面にイオン交換に寄与する官能基を備えているから、電解質膜としての性能を十分に発揮することができる。また、表面処理により膜の表面に所定形状の窪みが複数形成されているから、触媒との接触面積を多くすることができる。
【0014】
本発明の第2の固体高分子型燃料電池用の電解質膜は、
固体高分子型燃料電池に用いられる電解質膜であって、
強酸性陽イオン交換膜により形成され、
該強酸性陽イオン交換膜の少なくとも一方の面に10-6mのオーダーの所定形状の窪みを複数備える
ことを要旨とする。
【0015】
この本発明の第2の固体高分子型燃料電池用の電解質膜では、膜の表面に所定形状の窪みが複数形成されているから、触媒との接触面積を多くすることができる。
【0016】
こうした本発明の第2の固体高分子型燃料電池用の電解質膜において、前記強酸性陽イオン交換膜の前記所定形状の窪みが形成された近傍表面にイオン交換に寄与する官能基が配置されてなるものとすることもできる。こうすれば、電解質膜の性能を十分に発揮させることができる。
【0017】
【発明の実施の形態】
次に、本発明の実施の形態を実施例を用いて説明する。図1は本発明の一実施例である固体高分子型燃料電池用の電解質膜30の製造の様子を例示する製造工程図であり、図2は実施例の電解質膜30の製造の様子を模式的に示す製造模式図である。
【0018】
図示するように電解質膜30の製造は、まず、強酸性陽イオン交換膜22のプロトンを重金属に置換する工程から始まる(工程S10)。実施例では、イオン交換膜としてスルホン基を交換基とする強酸性陽イオン交換膜(DuPont社製のNafion122)を用い、電子染色技術により次式(1)に示すイオン交換反応によりスルホン基のプロトンを重金属(例えば、鉛や亜鉛,アルミニウム,鉄,白金など)で置換して、重金属で置換されたイオン交換膜24とした。なお、この置換は弱酸塩水溶液(例えば、酢酸鉛や酢酸亜鉛などの水溶液)に強酸性陽イオン交換膜22を浸漬することにより行なった。
【0019】
イオン交換反応: nRH++Mn+ ⇔ Rnn++nH+ (1)
【0020】
図3は強酸性陽イオン交換膜22を飽和酢酸亜鉛水溶液に浸漬してプロトンを亜鉛で置換したときの亜鉛とスルホン基とのクラスタ推定構造を示す説明図であり、図4は強酸性陽イオン交換膜22を飽和酢酸鉛水溶液に浸漬してプロトンを鉛で置換したときの鉛とスルホン基とのクラスタ推定構造を示す説明図である。図示するように、スルホン基にはプロトンに代わって重金属としての亜鉛や鉛が置換されている。
【0021】
次に、重金属で置換されたイオン交換膜24に対して放射線を照射して膜の表面に所定形状の窪み26をパターン形成する(工程S12)。イオン交換膜に放射線を照射すると、イオン交換膜は架橋して硬化するか、分解することが多い。強酸性陽イオン交換膜では放射線の照射は分解を促進するが、プロトンを重金属で置換すると、その強度が高くなり放射線によるイオン交換膜の劣化(分解)が抑制されるから、放射線を照射してもイオン交換膜の構造に変化は生じない。放射線としてはプラズマや電子線,X線,γ線などが含まれ、そのいずれでもパターン形成することができる。実施例では、強度などの制御が容易な電子線を用い、電子線リソグラフィーによりパターン形成を行なった。なお、パターン形成に電子線リソグラフィーを用いれば、膜の表面に10-6mオーダーの所望の形状の窪みを形成することができる。
【0022】
そして、重金属で置換されたイオン交換膜24に対して上述の式(1)のイオン交換反応の逆反応を用いて重金属をプロトンで置換して(工程S14)、電解質膜30を完成する。実施例では、重金属で置換されたイオン交換膜24を希硫酸に浸漬して重金属をプロトンに置換した。
【0023】
完成した電解質膜30は、その表面に10-6mオーダーの所定形状の窪み32を備えており、この所定形状の窪み32の形成された面の表面にはイオン交換基としてのスルホン基が変質や破壊されることなく存在する。なお、所定形状の窪み32は、断面が矩形や三角その他の多角形,円形,楕円形など如何なる形状であってもよい。
【0024】
以上説明した実施例の電解質膜30によれば、その表面に10-6mオーダーの所定形状の窪み32を備えるから、触媒との接触面積を大きく持つことができ、反応性の高い電解質膜とすることができる。また、実施例の電解質膜30によれば、所定形状の窪み32の形成された面の表面にはイオン交換基としてのスルホン基が変質や破壊されることなく存在するから、所定形状の窪み32の形成による膜表面の変質がなく、電解質膜の性能を十分に発揮することができる。
【0025】
以上説明した実施例の電解質膜30の製造方法によれば、触媒との接触面積が大きく、イオン交換性能を十分に発揮できる電解質膜を製造することができる。また、実施例の電解質膜30の製造方法によれば、強酸性陽イオン交換膜22のプロトンを重金属で置換した後に膜に放射線を照射してその表面に所定形状の窪み26を形成するから、放射線の照射によりイオン交換膜の分解やイオン交換基の変質,破壊を防止することができる。さらに、実施例の電解質膜30の製造方法によれば、放射線としてその強度などの制御が容易な電子線を用いたので、膜の表面に所望の形状の窪み26をパターン形成することができる。
【0026】
実施例の電解質膜30では、イオン交換膜として強酸性陽イオン交換膜22を用いたが、電解質膜として機能すれば弱酸性陽イオン交換膜などを用いてもよい。
【0027】
以上、本発明の実施の形態について実施例を用いて説明したが、本発明はこうした実施例に何等限定されるものではなく、本発明の要旨を逸脱しない範囲内において、種々なる形態で実施し得ることは勿論である。
【図面の簡単な説明】
【図1】 本発明の一実施例である固体高分子型燃料電池用の電解質膜30の製造の様子を例示する製造工程図である。
【図2】 実施例の電解質膜30の製造の様子を模式的に示す製造模式図である。
【図3】 強酸性陽イオン交換膜22を飽和酢酸亜鉛水溶液に浸漬してプロトンを亜鉛で置換したときの亜鉛とスルホン基とのクラスタ推定構造を示す説明図である。
【図4】 強酸性陽イオン交換膜22を飽和酢酸鉛水溶液に浸漬してプロトンを鉛で置換したときの鉛とスルホン基とのクラスタ推定構造を示す説明図である。
【符号の説明】
22 強酸性陽イオン交換膜、24 重金属で置換されたイオン交換膜、26所定形状の窪み、30 電解質膜、32 所定形状の窪み。
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an electrolyte membrane for a polymer electrolyte fuel cell and a method for producing the same.
[0002]
[Prior art]
Conventionally, as an electrolyte membrane for this type of polymer electrolyte fuel cell, a membrane obtained by subjecting the surface of the electrolyte membrane to surface roughening has been proposed (Japanese Patent Laid-Open No. 5-258756, etc.). In this electrolyte membrane, the reaction field of the electrochemical reaction occurring at the three-phase interface between the electrolyte membrane, the catalyst and the gas is deposited by depositing a metal as a catalyst in the concave and convex portions formed by surface roughening treatment applied to the surface. It is said that it is possible to improve the battery characteristics by increasing the utilization ratio of the catalyst and the battery characteristics.
[0003]
[Problems to be solved by the invention]
However, such an electrolyte membrane has a problem in that catalyst particles near the surface of the catalyst deposited in the recess only contribute to the electrochemical reaction, and many catalyst particles deposited in the recess do not contribute to the reaction. . Such a problem is accompanied by the problem of increasing the cost of a fuel cell using an electrolyte membrane when a noble metal is used as a catalyst.
[0004]
In addition, depending on the treatment method, the electrolyte membrane whose surface is roughened may be chemically altered or physically destroyed, and does not function effectively as an electrolyte membrane. There was also the problem of producing parts. Usually, an ion exchange membrane is used as the electrolyte membrane, but functional groups that contribute to ion exchange may be destroyed by chemical surface treatment or physical surface treatment. In this case, the function of ion exchange is lost, and the electrolyte The performance as a film is reduced.
[0005]
In order to solve some of these problems, the applicant applied plasma sputter etching to the electrolyte membrane surface to form irregularities on the film surface, and the catalyst layer has a substantially uniform thickness along the irregularities. Has been proposed (Japanese Patent Application No. 6-315502).
[0006]
An object of the electrolyte membrane for a polymer electrolyte fuel cell of the present invention is to increase the contact area with the catalyst without increasing the performance as an electrolyte membrane, thereby increasing the reactivity. An object of the method for producing an electrolyte membrane for a polymer electrolyte fuel cell of the present invention is to provide a method for producing an electrolyte membrane that can take a large contact area with a catalyst without deteriorating the performance as an electrolyte membrane.
[0007]
[Means for solving the problems and their functions and effects]
The electrolyte membrane for a polymer electrolyte fuel cell and the method for producing the same according to the present invention employs the following means in order to achieve at least a part of the above object.
[0008]
The method for producing an electrolyte membrane for a polymer electrolyte fuel cell according to the present invention includes:
A method for producing an electrolyte membrane used in a polymer electrolyte fuel cell,
A heavy metal substitution step of substituting protons of the cation exchange membrane with heavy metals;
A surface treatment step of performing surface treatment to irradiate at least one surface of the substituted cation exchange membrane to form a plurality of depressions having a predetermined shape on the surface;
And a proton substitution step for substituting the heavy metal of the surface-treated cation exchange membrane with protons.
[0009]
In the method for producing an electrolyte membrane for a polymer electrolyte fuel cell according to the present invention, the protons of the cation exchange membrane are replaced with heavy metals to prevent functional groups that contribute to ion exchange from being altered or destroyed during surface treatment. can do. As a result, the performance of the electrolyte membrane is not deteriorated by the surface treatment. Moreover, since a plurality of depressions having a predetermined shape are formed on the surface of the film by the surface treatment, the contact area with the catalyst can be increased. Here, “radiation” includes plasma, electron beam, X-ray, γ-ray and the like. Further, “heavy metal” includes lead, zinc, aluminum, iron, platinum and the like.
[0010]
In such a method for producing an electrolyte membrane for a polymer electrolyte fuel cell of the present invention, a strongly acidic cation exchange membrane may be used as the cation exchange membrane. In the method for producing an electrolyte membrane for a polymer electrolyte fuel cell of the present invention, the heavy metal substitution step may be a step of substitution using a weak acid salt aqueous solution of the heavy metal. Here, the “heavy salt aqueous solution of heavy metal” includes an aqueous solution of a heavy metal salt with acetic acid (for example, an aqueous solution of lead acetate, zinc acetate, or the like).
[0011]
In the method for producing an electrolyte membrane for a polymer electrolyte fuel cell of the present invention, the surface treatment step may be a step performed using an electron beam as the radiation. Since the electron beam is easy to control, a depression having a predetermined shape can be easily formed on the surface of the film. In addition, since the electron beam is obtained at a lower cost than plasma, X-rays, and γ rays, the manufacturing cost of the electrolyte membrane can be reduced.
[0012]
The electrolyte membrane for the first polymer electrolyte fuel cell of the present invention is:
An electrolyte membrane used in a polymer electrolyte fuel cell,
Replacing protons of the cation exchange membrane with heavy metal, irradiating at least one surface of the substituted cation exchange membrane with a plurality of dents of a predetermined shape on the surface, the dent of the predetermined shape The gist of the present invention is that the heavy metal in a plurality of formed cation exchange membranes is replaced with protons.
[0013]
In the electrolyte membrane for the first polymer electrolyte fuel cell of the present invention, the proton of the cation exchange membrane is subjected to a surface treatment by replacing the heavy metal with a heavy metal, and a functional group contributing to ion exchange is provided on the surface of the surface-treated membrane. Since it is provided, the performance as the electrolyte membrane can be sufficiently exhibited. Further, since a plurality of depressions having a predetermined shape are formed on the surface of the film by the surface treatment, the contact area with the catalyst can be increased.
[0014]
The electrolyte membrane for the second polymer electrolyte fuel cell of the present invention is:
An electrolyte membrane used in a polymer electrolyte fuel cell,
Formed by a strongly acidic cation exchange membrane,
The gist is that a plurality of depressions having a predetermined shape of the order of 10 −6 m are provided on at least one surface of the strongly acidic cation exchange membrane.
[0015]
In the electrolyte membrane for the second polymer electrolyte fuel cell of the present invention, a plurality of depressions having a predetermined shape are formed on the surface of the membrane, so that the contact area with the catalyst can be increased.
[0016]
In such an electrolyte membrane for a second polymer electrolyte fuel cell of the present invention, a functional group contributing to ion exchange is disposed on the surface of the strongly acidic cation exchange membrane in the vicinity of which the depression having the predetermined shape is formed. It can also be. In this way, the performance of the electrolyte membrane can be sufficiently exhibited.
[0017]
DETAILED DESCRIPTION OF THE INVENTION
Next, embodiments of the present invention will be described using examples. FIG. 1 is a production process diagram illustrating the production of an electrolyte membrane 30 for a polymer electrolyte fuel cell according to one embodiment of the present invention, and FIG. 2 schematically illustrates the production of the electrolyte membrane 30 of the embodiment. FIG.
[0018]
As shown in the drawing, the production of the electrolyte membrane 30 starts from a step of replacing protons of the strong acid cation exchange membrane 22 with heavy metals (step S10). In the examples, a strongly acidic cation exchange membrane (Nafion 122 manufactured by DuPont) having a sulfone group as an exchange group is used as the ion exchange membrane, and the proton of the sulfone group is obtained by an ion exchange reaction represented by the following formula (1) by an electron staining technique. Was replaced with heavy metal (for example, lead, zinc, aluminum, iron, platinum, etc.) to obtain an ion exchange membrane 24 substituted with heavy metal. This substitution was performed by immersing the strongly acidic cation exchange membrane 22 in an aqueous solution of a weak acid salt (for example, an aqueous solution of lead acetate, zinc acetate or the like).
[0019]
Ion exchange reaction: nRH + + M n + ⇔R n M n + + nH + (1)
[0020]
FIG. 3 is an explanatory view showing a cluster estimation structure of zinc and a sulfone group when the strongly acidic cation exchange membrane 22 is immersed in a saturated zinc acetate aqueous solution and protons are substituted with zinc, and FIG. 4 is a strongly acidic cation. It is explanatory drawing which shows the cluster estimation structure of lead and a sulfone group when the exchange membrane 22 is immersed in saturated lead acetate aqueous solution, and the proton is substituted with lead. As shown in the figure, the sulfone group is substituted with zinc or lead as heavy metals in place of protons.
[0021]
Next, the ion exchange membrane 24 substituted with heavy metal is irradiated with radiation to form a pattern of depressions 26 having a predetermined shape on the surface of the membrane (step S12). When an ion exchange membrane is irradiated with radiation, the ion exchange membrane is often crosslinked and cured or decomposed. In strong acidic cation exchange membranes, irradiation promotes decomposition, but if protons are replaced with heavy metals, the intensity of the protons increases and the deterioration (decomposition) of the ion exchange membrane due to radiation is suppressed. However, the structure of the ion exchange membrane does not change. Radiation includes plasma, electron beam, X-ray, γ-ray, etc., and any of them can form a pattern. In the examples, pattern formation was performed by electron beam lithography using an electron beam whose intensity and the like can be easily controlled. If electron beam lithography is used for pattern formation, a depression having a desired shape on the order of 10 −6 m can be formed on the surface of the film.
[0022]
Then, the heavy metal is replaced with a proton using the reverse reaction of the ion exchange reaction of the above formula (1) for the ion exchange membrane 24 replaced with the heavy metal (step S14), and the electrolyte membrane 30 is completed. In the example, the heavy metal substituted ion exchange membrane 24 was immersed in dilute sulfuric acid to replace the heavy metal with protons.
[0023]
The completed electrolyte membrane 30 is provided with a depression 32 having a predetermined shape on the order of 10 −6 m on the surface, and a sulfone group as an ion exchange group is altered on the surface of the surface where the depression 32 having the predetermined shape is formed. It exists without being destroyed. The recess 32 having a predetermined shape may have any shape such as a rectangle, a triangle, other polygons, a circle, or an ellipse.
[0024]
According to the electrolyte membrane 30 of the embodiment described above, the depression 32 having a predetermined shape on the order of 10 −6 m is provided on the surface thereof, so that the contact area with the catalyst can be increased, and the highly reactive electrolyte membrane and can do. Further, according to the electrolyte membrane 30 of the embodiment, since the sulfone group as the ion exchange group is present on the surface of the surface where the recess 32 of the predetermined shape is formed without being altered or destroyed, the recess 32 of the predetermined shape. The membrane surface is not altered by the formation of the film, and the performance of the electrolyte membrane can be fully exhibited.
[0025]
According to the manufacturing method of the electrolyte membrane 30 of the embodiment described above, an electrolyte membrane that has a large contact area with the catalyst and can sufficiently exhibit the ion exchange performance can be manufactured. Further, according to the method of manufacturing the electrolyte membrane 30 of the embodiment, the proton of the strong acid cation exchange membrane 22 is replaced with heavy metal, and then the membrane is irradiated with radiation to form a recess 26 having a predetermined shape on the surface. Irradiation can prevent the ion exchange membrane from being decomposed and ion exchange groups from being altered or destroyed. Furthermore, according to the manufacturing method of the electrolyte membrane 30 of the embodiment, since an electron beam whose intensity is easily controlled is used as the radiation, the depressions 26 having a desired shape can be formed in a pattern on the surface of the membrane.
[0026]
In the electrolyte membrane 30 of the embodiment, the strong acid cation exchange membrane 22 is used as the ion exchange membrane, but a weak acid cation exchange membrane or the like may be used as long as it functions as an electrolyte membrane.
[0027]
The embodiments of the present invention have been described using the embodiments. However, the present invention is not limited to these embodiments, and can be implemented in various forms without departing from the gist of the present invention. Of course you get.
[Brief description of the drawings]
FIG. 1 is a manufacturing process diagram illustrating the production of an electrolyte membrane 30 for a polymer electrolyte fuel cell according to an embodiment of the present invention.
FIG. 2 is a production schematic diagram schematically showing the production of the electrolyte membrane 30 of the example.
FIG. 3 is an explanatory diagram showing a cluster estimation structure of zinc and a sulfone group when a strongly acidic cation exchange membrane 22 is immersed in a saturated zinc acetate aqueous solution and protons are substituted with zinc.
FIG. 4 is an explanatory diagram showing a cluster estimation structure of lead and sulfone groups when a strongly acidic cation exchange membrane 22 is immersed in a saturated aqueous lead acetate solution to replace protons with lead.
[Explanation of symbols]
22 strong acid cation exchange membrane, 24 ion exchange membrane substituted with heavy metal, 26 depression of predetermined shape, 30 electrolyte membrane, 32 depression of predetermined shape.

Claims (4)

固体高分子型燃料電池に用いられる電解質膜の製造方法であって、
陽イオン交換膜のプロトンを鉛又は亜鉛で置換する重金属置換工程と、
該置換された陽イオン交換膜の少なくとも一方の面に放射線を照射して該面に所定形状の窪みを複数形成する表面処理を行なう表面処理工程と、
該表面処理された陽イオン交換膜の前記鉛又は前記亜鉛をプロトンに置換するプロトン置換工程と
を備える電解質膜の製造方法。
A method for producing an electrolyte membrane used in a polymer electrolyte fuel cell,
A heavy metal substitution step of substituting the protons of the cation exchange membrane with lead or zinc ;
A surface treatment step of performing surface treatment to irradiate at least one surface of the substituted cation exchange membrane to form a plurality of depressions having a predetermined shape on the surface;
And a proton substitution step of substituting the lead or zinc of the surface-treated cation exchange membrane with protons.
前記陽イオン交換膜として強酸性陽イオン交換膜を用いる請求項1記載の電解質膜の製造方法。  The method for producing an electrolyte membrane according to claim 1, wherein a strongly acidic cation exchange membrane is used as the cation exchange membrane. 前記重金属置換工程は、前記鉛又は前記亜鉛の弱酸塩水溶液を用いて置換する工程である請求項1または2記載の電解質膜の製造方法。The method for producing an electrolyte membrane according to claim 1 or 2 , wherein the heavy metal substitution step is a step of substitution using a weak salt aqueous solution of lead or zinc . 前記表面処理工程は、前記放射線として電子線を用いて行なう工程である請求項1ないしいずれか記載の電解質膜の製造方法。The surface treatment step is a manufacturing method of the electrolyte membrane according to any one of claims 1 to 3 is a step performed using an electron beam as the radiation.
JP05057999A 1999-02-26 1999-02-26 Method for producing electrolyte membrane for polymer electrolyte fuel cell Expired - Fee Related JP4337162B2 (en)

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