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JP2003082488A - Membrane electrode assembly and manufacturing method thereof - Google Patents

Membrane electrode assembly and manufacturing method thereof

Info

Publication number
JP2003082488A
JP2003082488A JP2001273186A JP2001273186A JP2003082488A JP 2003082488 A JP2003082488 A JP 2003082488A JP 2001273186 A JP2001273186 A JP 2001273186A JP 2001273186 A JP2001273186 A JP 2001273186A JP 2003082488 A JP2003082488 A JP 2003082488A
Authority
JP
Japan
Prior art keywords
membrane
electrode assembly
electrolyte membrane
solid polymer
polymer electrolyte
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2001273186A
Other languages
Japanese (ja)
Inventor
Michiko Horiguchi
道子 堀口
Mikimasa Yamaguchi
幹昌 山口
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Fuji Electric Co Ltd
Original Assignee
Fuji Electric Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Fuji Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP2001273186A priority Critical patent/JP2003082488A/en
Publication of JP2003082488A publication Critical patent/JP2003082488A/en
Pending legal-status Critical Current

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Classifications

    • 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

Landscapes

  • Fuel Cell (AREA)
  • Electrodes For Compound Or Non-Metal Manufacture (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Abstract

(57)【要約】 【課題】 固体高分子電解質膜を補強して製造過程にお
ける膜の損傷防止を図り、温水環境や高温加湿環境下に
おいても、電気化学的な特性を損なうことのない膜電極
接合体とその製造方法を提供する。 【解決手段】 電解質膜1の中央部両主面に触媒電極層
3,4を接合してなる電気化学装置用の膜電極接合体に
おいて、触媒電極層を接合していない電解質膜の外周面
部に額縁状に、樹脂を溶融固化して形成した補強層2を
設けてなるものとし、上記膜電極接合体の製造方法にお
いて、前記補強層2は、樹脂溶液を、電解質膜1の外周
面部に額縁状に塗布した後、乾燥して形成することとす
るか、もしくは、補強層2は、樹脂粉末を、電解質膜1
の外周面部に額縁状に散布し、この樹脂粉末層を加圧加
熱により溶融固化して形成する。
PROBLEM TO BE SOLVED: To provide a membrane electrode which does not impair electrochemical characteristics even in a hot water environment or a high-temperature humidified environment by reinforcing a solid polymer electrolyte membrane to prevent the membrane from being damaged in a manufacturing process. Provided is a joined body and a manufacturing method thereof. SOLUTION: In a membrane electrode assembly for an electrochemical device in which catalyst electrode layers 3 and 4 are bonded to both main surfaces of a central portion of an electrolyte membrane 1, an outer peripheral surface portion of an electrolyte membrane to which no catalyst electrode layer is bonded is provided. A reinforcing layer 2 formed by melting and solidifying a resin is provided in a frame shape. In the method for manufacturing a membrane / electrode assembly, the reinforcing layer 2 may be formed by applying a resin solution to the outer peripheral surface of the electrolyte membrane 1. After being applied in a shape, it may be formed by drying, or the reinforcing layer 2 may be formed by applying a resin powder to the electrolyte membrane 1.
The resin powder layer is formed by melting and solidifying the resin powder layer by heating under pressure.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】この発明は、固体高分子電解
質膜の中央部両主面に触媒電極層を接合してなる電気化
学装置用の膜電極接合体とその製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a membrane electrode assembly for an electrochemical device in which a catalyst electrode layer is joined to both main surfaces of a central portion of a solid polymer electrolyte membrane and a method for producing the same.

【0002】[0002]

【従来の技術】固体高分子電解質膜は、燃料電池,水電
解装置,食塩電解装置,塩酸電解装置,オゾン水製造装
置,酸素または水素の分離装置,各種ガスセンサー等の
電気化学装置用の膜電極接合体として広く用いられてお
り、代表的な例としてペルフルオロカーボンスルホン酸
膜が上げられる。製品としてはNafion(米国DuPont社の
商品名)、Aciplex(旭化成株式会社の商品名)、Fulem
ion(旭硝子株式会社の商品名)等がある。
Solid polymer electrolyte membranes are membranes for electrochemical devices such as fuel cells, water electrolyzers, salt electrolyzers, hydrochloric acid electrolyzers, ozone water production devices, oxygen or hydrogen separators, and various gas sensors. It is widely used as an electrode assembly, and a typical example thereof is a perfluorocarbon sulfonic acid film. Products include Nafion (trade name of DuPont, USA), Aciplex (trade name of Asahi Kasei Corporation), Fulem
ion (a product name of Asahi Glass Co., Ltd.) and the like.

【0003】前記電気化学装置用の膜電極接合体に関
し、本件発明の適用対象として最も好適な水電解装置を
代表例として、以下に述べる。
Regarding the above-mentioned membrane electrode assembly for an electrochemical device, the most suitable water electrolysis device to which the present invention is applied will be described below as a typical example.

【0004】水電解装置は、固体高分子電解質膜を隔膜
として陽極側と陰極側とに分離し、陽極側に純水、又は
イオンを含む水を供給しながら電気分解して、陽極側か
ら酸素ガスを、陰極側から水素ガスをそれぞれ発生する
ように構成したもので、そのシステム構成,スタックの
構造,運転方法等々に関して、種々の提案が行なわれて
いる(例えば、実開平2−51263号または実開平3
−74670号の全文明細書、特開平7−252682
号公報、特開平8−311676号公報、特開2000
−54175号公報など参照)。
A water electrolysis apparatus separates an anode side and a cathode side by using a solid polymer electrolyte membrane as a diaphragm, and electrolyzes while supplying pure water or water containing ions to the anode side, and oxygen is discharged from the anode side. The gas is configured to generate hydrogen gas from the cathode side, and various proposals have been made regarding the system configuration, stack structure, operating method, etc. (for example, Japanese Utility Model Laid-Open No. 2-51263 or Actual Kaihei 3
-74670 full-text specification, JP-A-7-252682
Japanese Unexamined Patent Publication No. Hei 8-311676, Japanese Unexamined Patent Publication No. 2000
-54175 gazette etc.).

【0005】前記実開平3−74670号の全文明細書
には、模式的な水電解セルの構成が開示されており、図
3にその概要を示す。図3に示す水電解セルは、固体高
分子電解質膜24の両主面に触媒電極20,21を接合
してなる膜電極接合体と、その両側に設けた多孔性の集
電体18,19と、さらにその両側に設けた通電用の端
子板22,23とからなり、固体高分子電解質膜24で
仕切られた陽極室13と陰極室14とにより水電解セル
が構成されている。
The full-text specification of the above-mentioned Japanese Utility Model Publication No. 3-74670 discloses a schematic structure of a water electrolysis cell, which is shown in FIG. The water electrolysis cell shown in FIG. 3 includes a membrane electrode assembly in which catalyst electrodes 20 and 21 are joined to both main surfaces of a solid polymer electrolyte membrane 24, and porous current collectors 18 and 19 provided on both sides thereof. And the terminal plates 22 and 23 for energization provided on both sides thereof, and the anode chamber 13 and the cathode chamber 14 partitioned by the solid polymer electrolyte membrane 24 form a water electrolysis cell.

【0006】上記構成において、供給水入口15から陽
極室13へ水を供給し、端子板22,23間に直流電圧
を加えることにより、水の電気分解が起こり、陽極室1
3において酸素ガスが発生し、同時に生成した水素イオ
ンH+が固体高分子電解質膜24を通って陰極室14へ
向い、水素イオンH+が陰極から電子を得て水素ガスH2
が発生する。部番16で示すポートからこの水素ガスと
水とが排出され、また、部番17で示すポートから酸素
ガスと水とが排出される。前記水電解セルの運転温度
は、60〜90℃、通常80℃である。
In the above structure, by supplying water from the feed water inlet 15 to the anode chamber 13 and applying a DC voltage between the terminal plates 22 and 23, electrolysis of the water occurs and the anode chamber 1
3, oxygen gas is generated, and simultaneously generated hydrogen ions H + pass through the solid polymer electrolyte membrane 24 toward the cathode chamber 14, and hydrogen ions H + acquire electrons from the cathode to generate hydrogen gas H 2
Occurs. The hydrogen gas and water are discharged from the port indicated by part number 16, and the oxygen gas and water are discharged from the port indicated by part number 17. The operating temperature of the water electrolysis cell is 60 to 90 ° C, usually 80 ° C.

【0007】前記触媒電極20,21と固体高分子電解
質膜24とからなる膜電極接合体は、水電解装置以外の
電気化学装置においても、概ね同様の構成となってお
り、例えば、以下のような手順により製造される。図2
は、膜電極接合体の製造手順の概要を説明する模式図を
示し、図2(a)は接合前の状態、図2(b)は接合後
の状態を示す。
The membrane electrode assembly comprising the catalyst electrodes 20 and 21 and the solid polymer electrolyte membrane 24 has substantially the same structure in electrochemical devices other than the water electrolysis device. Manufactured by various procedures. Figure 2
2A and 2B are schematic diagrams for explaining the outline of the manufacturing procedure of the membrane electrode assembly, in which FIG. 2A shows a state before joining and FIG. 2B shows a state after joining.

【0008】図2(a)に示すように、触媒電極層(陽
極)3と触媒電極層(陰極)4とを形成したPTFEシ
ート5により、電解質膜1を挟み、接合治具に組み込ん
だ後、加熱加圧して、触媒電極層と電解質膜とを接合す
る。ここで、加熱温度および加圧力は、例えば、180
℃および20MPaである。上記のようにして接合後、接
合治具から取り外し、PTFEシート5を剥離し、図2
(b)に示す電解質膜の両面に触媒電極層が形成された
膜電極接合体を得る。
As shown in FIG. 2 (a), after the electrolyte membrane 1 is sandwiched by the PTFE sheet 5 having the catalyst electrode layer (anode) 3 and the catalyst electrode layer (cathode) 4, it is assembled in a joining jig. By heating and pressurizing, the catalyst electrode layer and the electrolyte membrane are bonded. Here, the heating temperature and the pressure are, for example, 180
° C and 20 MPa. After joining as described above, it is removed from the joining jig and the PTFE sheet 5 is peeled off.
A membrane electrode assembly having catalyst electrode layers formed on both surfaces of the electrolyte membrane shown in (b) is obtained.

【0009】この膜電極接合体に用いられる固体高分子
電解質膜としての前記ペルフルオロカーボンスルホン酸
膜は、電気化学的には良好な性能を有するが、膜厚が薄
いため破損しやすい問題がある。
The perfluorocarbon sulfonic acid membrane as a solid polymer electrolyte membrane used in this membrane electrode assembly has good electrochemical performance, but has a problem that it is easily damaged due to its small thickness.

【0010】例えば、図2(b)に示す膜電極接合体を
複数個用いて、集電体とともにスタックを構成する場
合、通常、額縁状に触媒電極層を包囲するシール材を介
挿して組み立てられる。前述のように、電解質膜の機械
強度が小さい場合、前記酸素ガスおよび水素ガスの差圧
および機械的ストレスにより、電解質膜が、特に、シー
ル材の近傍で破損することがある。
For example, when a plurality of membrane electrode assemblies shown in FIG. 2 (b) are used to form a stack together with a current collector, the assembly is usually assembled by inserting a sealing material surrounding the catalyst electrode layer in a frame shape. To be As described above, when the mechanical strength of the electrolyte membrane is low, the electrolyte membrane may be damaged especially in the vicinity of the sealing material due to the pressure difference between the oxygen gas and the hydrogen gas and the mechanical stress.

【0011】この固体高分子電解質膜の補強方法とし
て、従来、PTFEなどの含フッ素重合体からなる織布
を膜中に挿入する方法、PTFEフィブリル化繊維を充
填する方法、電極周辺部に額縁状の樹脂膜を熱融着する
方法(特開平5−234606号公報参照)、電極周辺
部に額縁状の粘着剤付樹脂シートを貼り付ける方法(特
開平10−154521号公報参照)等が知られてい
る。
As a method of reinforcing this solid polymer electrolyte membrane, conventionally, a method of inserting a woven fabric made of a fluoropolymer such as PTFE into the membrane, a method of filling the PTFE fibrillated fiber, and a frame shape around the electrode are used. There is known a method of heat-sealing the resin film (see JP-A-5-234606), a method of attaching a frame-shaped resin sheet with an adhesive to the peripheral portion of the electrode (see JP-A-10-154521). ing.

【0012】[0012]

【発明が解決しようとする課題】ところで、前記従来の
固体高分子電解質膜の補強方法においては、下記のよう
な問題がある。
However, the conventional methods for reinforcing a solid polymer electrolyte membrane described above have the following problems.

【0013】まず、電解質膜内にPTFE等の織布を挿
入する方法の場合、電解質膜の表面に織布による僅かな
凹凸を生じるため触媒電極層が均一に接合できず、電気
的接触抵抗が高くなって電気化学的特性が低下する問題
がある。
First, in the case of a method of inserting a woven cloth such as PTFE into the electrolyte membrane, slight unevenness due to the woven cloth is generated on the surface of the electrolyte membrane, so that the catalyst electrode layers cannot be evenly bonded and the electrical contact resistance is reduced. There is a problem that it becomes higher and the electrochemical characteristics deteriorate.

【0014】また、電解質膜内にPTFEフィブリル化
繊維を充填する方法の場合、イオン伝導性が落ちるため
セル電圧が上昇し、同様に電気化学的特性が低下する。
Further, in the case of the method of filling the PTFE fibrillated fiber in the electrolyte membrane, the ionic conductivity is lowered, so that the cell voltage is increased and similarly the electrochemical characteristics are lowered.

【0015】さらに、電極周辺部に額縁状の樹脂膜を熱
融着した場合、特に、水電解装置に適用した場合には、
電解質膜が60〜90℃の温水環境に晒されることとな
るので、電解質膜と額縁状の樹脂膜との伸び率の差によ
り、電解質膜の膨潤(約10%)に伴い触媒電極部分に
皺が発生し、電解特性などの電気化学的特性が低下する
問題がある。
Further, when a frame-shaped resin film is heat-sealed around the electrodes, particularly when applied to a water electrolysis device,
Since the electrolyte membrane is exposed to a hot water environment of 60 to 90 ° C., the catalyst electrode portion is wrinkled due to the swelling (about 10%) of the electrolyte membrane due to the difference in elongation between the electrolyte membrane and the frame-shaped resin membrane. Occurs, and electrochemical characteristics such as electrolytic characteristics deteriorate.

【0016】さらにまた、電極周辺部に額縁状の粘着剤
付樹脂シートを貼り付ける方法の場合に、伸び率を材質
的にある程度調整したとしても、固体高分子電解質膜の
伸延方向と樹脂シートの伸延方向とが異なる部分が生ず
るので、皺が発生して電解特性が低下する問題を解消し
得ない。
Furthermore, in the case of a method of attaching a frame-shaped resin sheet with an adhesive to the periphery of the electrode, even if the elongation is adjusted to some extent in terms of material, the direction of extension of the solid polymer electrolyte membrane and the resin sheet Since a portion different from the extending direction occurs, it is impossible to solve the problem that wrinkles occur and the electrolytic characteristics are deteriorated.

【0017】また、水電解装置に限らず、温水環境に晒
されない固体高分子型燃料電池のような電気化学装置に
おいても、60〜90℃程度の高温加湿環境下にあるの
で、程度の差はあるものの、前記と同様の問題がある。
Further, not only the water electrolysis device but also an electrochemical device such as a polymer electrolyte fuel cell which is not exposed to a hot water environment is under a high temperature humidification environment of about 60 to 90 ° C., and therefore there is a difference in degree. However, there is a problem similar to the above.

【0018】この発明は、上記のような問題点を解消す
るためになされたもので、本発明の課題は、固体高分子
電解質膜を補強して製造過程における膜の損傷防止を図
り、温水環境や高温加湿環境下においても、電気化学的
な特性を損なうことのない膜電極接合体とその製造方法
を提供することにある。
The present invention has been made to solve the above problems, and an object of the present invention is to reinforce a solid polymer electrolyte membrane to prevent the membrane from being damaged in the manufacturing process and to provide a hot water environment. Another object of the present invention is to provide a membrane / electrode assembly and a method for producing the same, which does not impair the electrochemical characteristics even under a high temperature and humid environment.

【0019】[0019]

【課題を解決するための手段】前述の課題を解決するた
め、この発明は、固体高分子電解質膜の中央部両主面に
触媒電極層を接合してなる電気化学装置用の膜電極接合
体において、触媒電極層を接合していない前記固体高分
子電解質膜の外周面部に額縁状に、樹脂を溶融固化して
形成した補強層を設けてなるものとする(請求項1の発
明)。
In order to solve the above-mentioned problems, the present invention provides a membrane electrode assembly for an electrochemical device in which a catalyst electrode layer is joined to both central surfaces of a solid polymer electrolyte membrane. In the invention, a reinforcing layer formed by melting and solidifying a resin is provided in a frame shape on the outer peripheral surface portion of the solid polymer electrolyte membrane to which the catalyst electrode layer is not joined (the invention of claim 1).

【0020】上記によれば、固体高分子電解質膜は補強
層を有するので、膜電極接合体の製作過程等での損傷が
防止できる。また、樹脂を溶融固化して形成した補強層
は、伸びに対して等方性を有するので、温水環境や高温
加湿環境下において、膜電極接合体に皺が発生する問題
が解消され、安定した電気化学的特性が維持できる。
According to the above, since the solid polymer electrolyte membrane has the reinforcing layer, it is possible to prevent damage during the manufacturing process of the membrane electrode assembly. In addition, since the reinforcing layer formed by melting and solidifying the resin is isotropic with respect to elongation, the problem of wrinkles occurring in the membrane electrode assembly is eliminated and stabilized in a hot water environment or a high temperature humidified environment. The electrochemical characteristics can be maintained.

【0021】前記請求項1の発明の適用対象としては、
固体高分子電解質膜が温水環境に晒される水電解装置が
最適である。即ち、請求項1に記載の膜電極接合体にお
いて、前記電気化学装置は、水電解装置とする(請求項
2の発明)。
The subject matter of the invention of claim 1 is as follows:
A water electrolysis device in which the solid polymer electrolyte membrane is exposed to a hot water environment is optimal. That is, in the membrane electrode assembly according to claim 1, the electrochemical device is a water electrolysis device (the invention of claim 2).

【0022】また、前記膜電極接合体を製造する方法と
しては、下記請求項3ないし6の発明が好ましい。即
ち、請求項1または2に記載の膜電極接合体の製造方法
において、前記補強層は、樹脂溶液を、前記固体高分子
電解質膜の外周面部に額縁状に塗布した後、乾燥して形
成する(請求項3の発明)。
As a method for producing the membrane electrode assembly, the inventions of claims 3 to 6 below are preferable. That is, in the method for producing a membrane electrode assembly according to claim 1 or 2, the reinforcing layer is formed by applying a resin solution to the outer peripheral surface of the solid polymer electrolyte membrane in a frame shape and then drying the resin solution. (Invention of Claim 3).

【0023】さらに、請求項3に記載の製造方法におい
て、前記樹脂溶液は、前記固体高分子電解質膜用の電解
質溶液とする(請求項4の発明)。請求項4の発明によ
れば、電解質膜と額縁状の樹脂膜との伸び率が同等とな
るので、膨潤に対する追随性の観点から最も好適とな
る。
Further, in the manufacturing method according to claim 3, the resin solution is an electrolyte solution for the solid polymer electrolyte membrane (invention of claim 4). According to the invention of claim 4, since the elongation rates of the electrolyte membrane and the frame-shaped resin membrane are equal to each other, it is most suitable from the viewpoint of followability to swelling.

【0024】また、前記請求項3ないし4の発明とは異
なる製造方法として、寸法精度向上の観点から下記請求
項5の発明が好ましい。即ち、請求項1または2に記載
の膜電極接合体の製造方法において、前記補強層は、樹
脂粉末を、前記固体高分子電解質膜の外周面部に額縁状
に散布し、この樹脂粉末層を加圧加熱により溶融固化し
て形成する。
Further, as a manufacturing method different from the inventions of claims 3 to 4, the invention of claim 5 is preferable from the viewpoint of improving dimensional accuracy. That is, in the method for producing a membrane electrode assembly according to claim 1 or 2, the reinforcing layer is formed by dispersing resin powder in a frame shape on the outer peripheral surface of the solid polymer electrolyte membrane, and adding the resin powder layer. It is formed by melting and solidifying by pressure heating.

【0025】[0025]

【発明の実施の形態】図1に基づき、この発明の実施の
形態について以下に述べる。なお、各図1において、図
1(a)は接合前の状態、図1(b)は触媒電極層接合
後の状態、図1(c)は補強層形成後の状態を示し、図
2に示す部材と同一の機能を有する部材には、同一番号
を付して詳細説明を省略する。
BEST MODE FOR CARRYING OUT THE INVENTION An embodiment of the present invention will be described below with reference to FIG. 1A and 1B show the state before joining, FIG. 1B shows the state after joining the catalyst electrode layers, and FIG. 1C shows the state after forming the reinforcing layer. Members having the same functions as those shown are given the same reference numerals and detailed description thereof will be omitted.

【0026】図1において、図2と異なる点は、図1に
おいては、触媒電極層3,4を接合していない固体高分
子電解質膜1の外周面部に額縁状に、樹脂を溶融固化し
て形成した補強層2を設けた点である。
1 is different from FIG. 2 in that, in FIG. 1, the resin is melted and solidified in a frame shape on the outer peripheral surface of the solid polymer electrolyte membrane 1 where the catalyst electrode layers 3 and 4 are not joined. The point is that the formed reinforcing layer 2 is provided.

【0027】[0027]

【実施例】前記図1に示す実施の形態の製造方法に関わ
り、樹脂溶液を塗布する実施例と、樹脂粉末を加圧加熱
により溶融固化する実施例とについて、以下に述べる。
[Examples] Examples relating to the manufacturing method of the embodiment shown in FIG. 1 in which a resin solution is applied and examples in which resin powder is melted and solidified by heating under pressure are described below.

【0028】(実施例1)電気化学装置で用いる膜電極
接合体の、触媒を接合していない触媒層の外周部分の電
解質膜上に、市販の電解質溶液(ペルフルオロカーボン
スルホン酸の溶液)を2倍に濃縮した溶液(濃度10
%、水:エタノール=1:1)を刷毛塗りし、室温乾燥し
た。乾燥後、反対側の面に同様に溶液を塗布し、室温乾
燥した。前記塗布・乾燥を3回繰り返し外周面部分を補
強し、額縁状の補強層を形成した。補強なしの図2の従
来方法による膜電極接合体の試料は、電解質膜の周辺部
に破損が検出されたが、補強した膜電極接合体の試料に
は、破損が検出されなかった。
Example 1 A commercially available electrolyte solution (a solution of perfluorocarbon sulfonic acid) was added onto the electrolyte membrane around the outer periphery of the catalyst layer where the catalyst was not joined in the membrane electrode assembly used in the electrochemical device. Double concentrated solution (concentration 10
%, Water: ethanol = 1: 1), and the mixture was dried at room temperature. After drying, the solution was similarly applied to the opposite surface and dried at room temperature. The coating and drying were repeated three times to reinforce the outer peripheral surface portion to form a frame-shaped reinforcing layer. In the sample of the membrane electrode assembly according to the conventional method of FIG. 2 without reinforcement, damage was detected in the peripheral portion of the electrolyte membrane, but in the sample of the reinforced membrane electrode assembly, no damage was detected.

【0029】また、上記補強した膜電極接合体と、補強
なしの図2の従来方法による膜電極接合体について、8
0℃の温水中に15分浸漬して電解質膜を膨潤させた
後、念のため、初期電解特性を比較測定した。その結果
によれば、補強有り、無しのいずれの場合も、セル電圧
1.537V,電流効率99%,エネルギー効率95.
2%であり、補強層を設けたことによる初期特性への影
響は無いことが確認された。
The reinforced membrane electrode assembly and the non-reinforced membrane electrode assembly according to the conventional method shown in FIG.
After being immersed in warm water of 0 ° C. for 15 minutes to swell the electrolyte membrane, the initial electrolytic characteristics were comparatively measured just in case. According to the result, the cell voltage is 1.537 V, the current efficiency is 99%, the energy efficiency is 95.
It was 2%, and it was confirmed that the provision of the reinforcing layer did not affect the initial characteristics.

【0030】(実施例2)電気化学装置で用いる膜電極
接合体の、触媒を接合していない触媒層の外周部分の電
解質膜上に、低密度ポリエチレン粉末を5mg/cm2
で分散、外周部分のみを0.5MPa、100℃で加圧加熱
し外周面部分を補強した。補強した膜電極接合体の試料
には、破損が検出されなかった。
(Example 2) 5 mg / cm 2 of low-density polyethylene powder was placed on the electrolyte membrane in the outer peripheral portion of the catalyst layer where the catalyst was not joined in the membrane electrode assembly used in the electrochemical device.
Then, only the outer peripheral portion was pressurized and heated at 0.5 MPa and 100 ° C. to reinforce the outer peripheral surface portion. No damage was detected in the reinforced membrane electrode assembly sample.

【0031】また、上記補強した膜電極接合体と、補強
なしの図2の従来方法による膜電極接合体について、8
0℃の温水中に15分浸漬して電解質膜を膨潤させた
後、念のため、初期電解特性を比較測定した。その結果
によれば、補強有り、無しのいずれの場合も、セル電圧
1.535V,電流効率99%,エネルギー効率95.
4%であり、補強層を設けたことによる初期特性への影
響は無いことが確認された。
Further, regarding the reinforced membrane electrode assembly and the membrane electrode assembly according to the conventional method of FIG. 2 without reinforcement, 8
After being immersed in warm water of 0 ° C. for 15 minutes to swell the electrolyte membrane, the initial electrolytic characteristics were comparatively measured just in case. According to the result, the cell voltage is 1.535 V, the current efficiency is 99%, the energy efficiency is 95.
It was 4%, and it was confirmed that the provision of the reinforcing layer did not affect the initial characteristics.

【0032】[0032]

【発明の効果】この発明によれば前述のように、固体高
分子電解質膜の中央部両主面に触媒電極層を接合してな
る電気化学装置用の膜電極接合体において、触媒電極層
を接合していない前記固体高分子電解質膜の外周面部に
額縁状に、樹脂を溶融固化して形成した補強層を設けて
なるものとし、また、上記膜電極接合体の製造方法にお
いて、前記補強層は、樹脂溶液を、前記固体高分子電解
質膜の外周面部に額縁状に塗布した後、乾燥して形成す
ることとするか、もしくは、前記補強層は、樹脂粉末
を、前記固体高分子電解質膜の外周面部に額縁状に散布
し、この樹脂粉末層を加圧加熱により溶融固化して形成
することとしたので、製造過程における膜の損傷防止を
図り、温水環境や高温加湿環境下においても、電気化学
的な特性を損なうことのない膜電極接合体が提供でき
る。
EFFECTS OF THE INVENTION According to the present invention, as described above, in the membrane electrode assembly for an electrochemical device in which the catalyst electrode layers are joined to both central surfaces of the solid polymer electrolyte membrane, the catalyst electrode layers are The outer peripheral surface of the unbonded solid polymer electrolyte membrane is frame-shaped, and a reinforcing layer formed by melting and solidifying a resin is provided, and in the method for manufacturing the membrane electrode assembly, the reinforcing layer is used. Is to be formed by applying a resin solution to the outer peripheral surface of the solid polymer electrolyte membrane in a frame shape and then drying it, or the reinforcing layer is formed of resin powder as the solid polymer electrolyte membrane. Since it was sprayed in a frame shape on the outer peripheral surface of the, and was formed by melting and solidifying this resin powder layer by pressurizing and heating, the film was prevented from being damaged in the manufacturing process, and even in a hot water environment or a high temperature and humid environment, The one that impairs the electrochemical characteristics No membrane electrode assembly can be provided.

【図面の簡単な説明】[Brief description of drawings]

【図1】この発明の膜電極接合体の製造手順の概要を説
明する模式図
FIG. 1 is a schematic diagram for explaining the outline of the manufacturing procedure of a membrane electrode assembly of the present invention.

【図2】従来の膜電極接合体の製造手順の概要を説明す
る模式図
FIG. 2 is a schematic diagram illustrating an outline of a conventional procedure for manufacturing a membrane electrode assembly.

【図3】水電解セルの模式的構成図FIG. 3 is a schematic configuration diagram of a water electrolysis cell.

【符号の説明】[Explanation of symbols]

1:電解質膜、2:補強層、3:触媒電極層(陽極)、
4:触媒電極層(陰極)、5:PTFEシート。
1: electrolyte membrane, 2: reinforcing layer, 3: catalyst electrode layer (anode),
4: Catalyst electrode layer (cathode), 5: PTFE sheet.

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4K011 CA06 DA01 4K021 AA01 BA02 DB43 5H026 AA06 CX05    ─────────────────────────────────────────────────── ─── Continued front page    F-term (reference) 4K011 CA06 DA01                 4K021 AA01 BA02 DB43                 5H026 AA06 CX05

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 固体高分子電解質膜の中央部両主面に触
媒電極層を接合してなる電気化学装置用の膜電極接合体
において、触媒電極層を接合していない前記固体高分子
電解質膜の外周面部に額縁状に、樹脂を溶融固化して形
成した補強層を設けてなることを特徴とする膜電極接合
体。
1. A membrane electrode assembly for an electrochemical device, comprising a catalyst electrode layer bonded to both main surfaces of a central portion of a solid polymer electrolyte membrane, wherein the solid polymer electrolyte membrane is not bonded to the catalyst electrode layer. A membrane-electrode assembly, comprising a frame-like reinforcing layer provided on the outer peripheral surface of the resin, the reinforcing layer being formed by melting and solidifying a resin.
【請求項2】 請求項1に記載の膜電極接合体におい
て、前記電気化学装置は、水電解装置とすることを特徴
とする膜電極接合体。
2. The membrane electrode assembly according to claim 1, wherein the electrochemical device is a water electrolysis device.
【請求項3】 請求項1または2に記載の膜電極接合体
の製造方法において、前記補強層は、樹脂溶液を、前記
固体高分子電解質膜の外周面部に額縁状に塗布した後、
乾燥して形成することを特徴とする膜電極接合体の製造
方法。
3. The method of manufacturing a membrane electrode assembly according to claim 1, wherein the reinforcing layer is formed by applying a resin solution to the outer peripheral surface of the solid polymer electrolyte membrane in a frame shape.
A method of manufacturing a membrane electrode assembly, which comprises drying and forming.
【請求項4】 請求項3に記載の製造方法において、前
記樹脂溶液は、前記固体高分子電解質膜用の電解質溶液
とすることを特徴とする膜電極接合体の製造方法。
4. The method for manufacturing a membrane electrode assembly according to claim 3, wherein the resin solution is an electrolyte solution for the solid polymer electrolyte membrane.
【請求項5】 請求項1または2に記載の膜電極接合体
の製造方法において、前記補強層は、樹脂粉末を、前記
固体高分子電解質膜の外周面部に額縁状に散布し、この
樹脂粉末層を加圧加熱により溶融固化して形成すること
を特徴とする膜電極接合体の製造方法。
5. The method for manufacturing a membrane electrode assembly according to claim 1, wherein the reinforcing layer sprays resin powder on the outer peripheral surface of the solid polymer electrolyte membrane in a frame shape to form a resin powder. A method for producing a membrane electrode assembly, which comprises melting and solidifying a layer by heating under pressure.
JP2001273186A 2001-09-10 2001-09-10 Membrane electrode assembly and manufacturing method thereof Pending JP2003082488A (en)

Priority Applications (1)

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Publication Number Publication Date
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Family

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