Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JP3100754B2 - Method for manufacturing electrochemical device using solid polymer electrolyte membrane - Google Patents
[go: Go Back, main page]

JP3100754B2 - Method for manufacturing electrochemical device using solid polymer electrolyte membrane - Google Patents

Method for manufacturing electrochemical device using solid polymer electrolyte membrane

Info

Publication number
JP3100754B2
JP3100754B2 JP04127484A JP12748492A JP3100754B2 JP 3100754 B2 JP3100754 B2 JP 3100754B2 JP 04127484 A JP04127484 A JP 04127484A JP 12748492 A JP12748492 A JP 12748492A JP 3100754 B2 JP3100754 B2 JP 3100754B2
Authority
JP
Japan
Prior art keywords
solid polymer
polymer electrolyte
electrolyte membrane
electrode
catalyst layer
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.)
Expired - Fee Related
Application number
JP04127484A
Other languages
Japanese (ja)
Other versions
JPH05325983A (en
Inventor
憲朗 光田
秀雄 前田
俊明 村橋
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.)
Mitsubishi Electric Corp
Original Assignee
Mitsubishi Electric Corp
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 Mitsubishi Electric Corp filed Critical Mitsubishi Electric Corp
Priority to JP04127484A priority Critical patent/JP3100754B2/en
Publication of JPH05325983A publication Critical patent/JPH05325983A/en
Application granted granted Critical
Publication of JP3100754B2 publication Critical patent/JP3100754B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

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)
  • Inert Electrodes (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】この発明は、燃料電池や電界槽お
よびガスセンサ等に使用される固体高分子電解質膜を用
いた電気化学デバイスの製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for manufacturing an electrochemical device using a solid polymer electrolyte membrane used for a fuel cell, an electric field tank, a gas sensor and the like.

【0002】[0002]

【従来の技術】固体高分子電解質膜に電極触媒層を取り
付けた電気化学デバイスは燃料電池や電界槽等に広く用
いられている。そしてこのような電気化学デバイスでは
電極触媒層の利用率を高めるために種々の製造方法が提
案されている。例えば特公平2−4987号公報で示さ
れるものでは、固体高分子電解質膜の表面を研磨材等を
用いて粗面化し、この部分に電極触媒層を固着すること
により、固体高分子電解質膜と電極触媒層との間の反応
界面を3次元的に拡大し、このことにより、電極触媒層
の利用効率を高めている。
2. Description of the Related Art Electrochemical devices in which an electrode catalyst layer is attached to a solid polymer electrolyte membrane are widely used in fuel cells, electric field tanks and the like. And in such an electrochemical device, various manufacturing methods have been proposed in order to increase the utilization rate of the electrode catalyst layer. For example, in Japanese Patent Publication No. 2-4987, the surface of the solid polymer electrolyte membrane is roughened using an abrasive or the like, and the electrode catalyst layer is fixed to this portion to form a solid polymer electrolyte membrane. The reaction interface between the electrode catalyst layer and the electrode catalyst layer is three-dimensionally enlarged, thereby increasing the use efficiency of the electrode catalyst layer.

【0003】また、特開平3−167752号公報で示
されるものでは、電極触媒層の表面をプレス治具にて凹
凸形状に仕上げ、この電極触媒層を固体高分子電解質膜
に密着させることにより、固体高分子電解質膜と電極触
媒層との間の反応界面を3次元的に拡大し、このことに
より、電極触媒層の利用効率を高めている。
[0003] Further, in Japanese Patent Application Laid-Open No. Hei 3-167752, the surface of an electrode catalyst layer is made uneven by a press jig, and the electrode catalyst layer is brought into close contact with a solid polymer electrolyte membrane. The reaction interface between the solid polymer electrolyte membrane and the electrode catalyst layer is three-dimensionally enlarged, thereby increasing the use efficiency of the electrode catalyst layer.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、上記従
来の電気化学デバイスでは、いずれについても、固体高
分子電解質膜が水分を吸収して大幅に膨張すると固体高
分子電解質膜と電極触媒層との3次元的反応界面が物理
的に外れて離れやすいという問題があった。このため、
このような電気化学デバイスでは固体高分子電解質膜が
吸湿しても膨張しないように、この電気化学デバイスの
動作いかんによらず、常時固体高分子電解質膜と電極触
媒層との間にかなりの面圧をかけておく必要があった。
また、上記電気化学デバイスでは、いずれも粗面化の工
程を必要とし、その製造作業も容易ではなかった。
However, in each of the above-mentioned conventional electrochemical devices, when the solid polymer electrolyte membrane absorbs moisture and expands significantly, the solid polymer electrolyte membrane and the electrode catalyst layer become three-dimensional. There is a problem that the dimensional reaction interface is physically separated and easily separated. For this reason,
In such an electrochemical device, a considerable surface is always present between the solid polymer electrolyte membrane and the electrode catalyst layer regardless of the operation of the electrochemical device so that the solid polymer electrolyte membrane does not expand even if it absorbs moisture. It needed to be under pressure.
In addition, all of the above-mentioned electrochemical devices require a roughening step, and the manufacturing operation thereof is not easy.

【0005】この発明は、上記のような課題を解決する
ためになされたものであり、固体高分子電解質膜と電極
触媒層との間に形成された3次元的な反応界面を特別な
操作をすることなく維持でき、かつ、製造作業も容易な
固体高分子電解質膜を用いた電気化学デバイスの製造方
法を提供することを目的とする。
The present invention has been made in order to solve the above-mentioned problems, and a special operation is performed on a three-dimensional reaction interface formed between a solid polymer electrolyte membrane and an electrode catalyst layer. It is an object of the present invention to provide a method of manufacturing an electrochemical device using a solid polymer electrolyte membrane that can be maintained without performing and easy to manufacture.

【0006】[0006]

【課題を解決するための手段】この発明に係る固体高分
子電解質膜を用いた電気化学デバイスの製造方法は、電
極触媒層を挟んでスルホン酸基をイオン交換基としても
つイオン性の固体高分子電解質膜と、電極触媒層より大
きく、かつ、固体高分子電解質膜より小さい面積を有す
電極基材とを130℃以上210℃未満の温度下でホ
ットプレスして、電極基材の表面を固体高分子電解質膜
内に30μm以上の深さまで食い込ませると供に、電極
基材全体を固体高分子電解質膜内に食い込ませたことを
特徴とする。
Means for Solving the Problems The method of manufacturing an electrochemical device using the solid polymer electrolyte membrane according to this inventions are ionic solid high having a sulfonic acid group as the ion exchange group to sandwich the electrode catalyst layer Larger than molecular electrolyte membrane and electrode catalyst layer
Crisp and has a smaller area than solid polymer electrolyte membrane
That with the electrode substrate and hot-pressed at a temperature of lower than 130 ° C. or higher 210 ° C., the surface of the electrode substrate to supply the Ru was bite to more depth 30μm solid polymer electrolyte in membrane electrode
It is characterized in that the entire base material is cut into the solid polymer electrolyte membrane .

【0007】[0007]

【0008】[0008]

【作用】この発明において、ホットプレスの温度を13
0℃以上210℃未満としたのは、固体高分子電解質膜
に熱分解を生じさせることなく電極基材を小さな面圧で
固体高分子電解質膜内に食い込ませることができるから
である。また、電極触媒層より大きく、かつ、固体高分
子電解質膜より小さい面積を有する電極基材の表面を固
体高分子電解質膜内に30μmの以上の厚さまで食い込
ませたのは、固体高分子電解質膜が吸湿して膨張しても
電極基材が固体高分子電解質膜側から一部外れたり、脱
落するのを防止するためであり、かつ、固体高分子電解
質膜と電極触媒層との間に3次元的な反応界面を形成す
るためである。さらに、電極基材全体を固体高分子電解
質膜内に食い込ませたのは、電極基材の固体高分子電解
質膜側からの外れや脱落を一層防止するためである。
In the present invention, the temperature of the hot press is set to 13
The reason why the temperature is set to 0 ° C. or higher and lower than 210 ° C. is that the electrode base material can be cut into the solid polymer electrolyte membrane with a small surface pressure without causing thermal decomposition of the solid polymer electrolyte membrane. Also, larger than the electrode catalyst layer, and solid high content
Was allowed bites to over a thickness of 30μm to a surface of the conductive Gokumoto material having a smaller area than the child electrolyte membrane solid polymer electrolyte in membrane, solid polymer electrolyte membrane hygroscopic to inflated electrode substrate be Is to prevent a part from coming off or falling off from the solid polymer electrolyte membrane side, and to form a three-dimensional reaction interface between the solid polymer electrolyte membrane and the electrode catalyst layer. . In addition, solid polymer electrolysis
The solid polymer electrolysis of the electrode substrate
This is to further prevent detachment or falling off from the membrane side.

【0009】[0009]

【0010】[0010]

【実施例】以下、この発明の実施例を図について説明す
る。 実施例1.図1はこの発明の第1の発明に係る一実施例
を示すホットプレス前の固体高分子電解質型電極を構成
する各部材の側面図、図2はホットプレスして形成され
た固体高分子電解質型電極の側断面図である。
BRIEF DESCRIPTION OF THE DRAWINGS FIG. Embodiment 1 FIG. FIG. 1 is a side view of members constituting a solid polymer electrolyte type electrode before hot pressing, showing an embodiment according to the first invention of the present invention, and FIG. 2 is a solid polymer electrolyte formed by hot pressing. It is a sectional side view of a pattern electrode.

【0011】図において、1はイオンは通すが電子は通
さない固体高分子電解質膜、2は厚さが50μm以下の
薄い電極触媒層、3は所定の温度では固体高分子電解質
膜1より硬い多孔質または空孔や隙間の多い導電性材料
からなる電極基材、4はその両面に電極触媒層2が置か
れた固体高分子電解質膜1を一対の電極基材3、3で挟
み付けてホットプレスし、電極基材3が固体高分子電解
質膜1の内方に30μm以上の深さまで食い込んでいる
電気化学デバイスとしての固体高分子電解質型電極であ
る。
In the figure, 1 is a solid polymer electrolyte membrane that allows ions to pass but does not allow electrons to pass through, 2 is a thin electrode catalyst layer having a thickness of 50 μm or less, and 3 is a porous membrane that is harder than the solid polymer electrolyte membrane 1 at a predetermined temperature. The electrode substrate 4 made of a conductive material having many pores or gaps is formed by sandwiching a solid polymer electrolyte membrane 1 having an electrode catalyst layer 2 on both surfaces thereof between a pair of electrode substrates 3 and 3. This is a solid polymer electrolyte type electrode as an electrochemical device in which the electrode substrate 3 is pressed into the solid polymer electrolyte membrane 1 to a depth of 30 μm or more.

【0012】ここで、固体高分子電解質膜1として使用
できるものは、スルホン酸基をイオン交換基としてもつ
イオン性の固体高分子電解質膜であり、例えばイー・ア
イ・デュポン社(E.I.Dupont de Num
ours & Co)からナフィオン(Nafion)
の商品名で販売されているスルホン化パーフルオロカー
ボン膜や、ダウ・ケミカル社(Dow Chemica
l Co.)から販売されている同様の膜がある。ま
た、電極触媒層2として使用できるものには、白金黒微
粒子とポリテトラフルオロエチレン樹脂の分散液および
固体高分子電解質膜を加水分解してイソプロピルアルコ
ールを主成分とする溶媒に溶解した液を混練して50μ
m以下の厚さに圧延した薄膜シート、または白金黒微粒
子の代わりに白金微粒子を担持した高表面積のカーボン
粉末を用いて作製された薄膜シート、または固体高分子
電解質膜1に直接無電解メッキされた白金微粒子層や固
体高分子電解質膜1に物理的に付着した白金粒子等があ
る。さらに、電極基材3として使用できるものには、多
孔質なカーボンペーパや白金メッキしたチタン製のエキ
スパンドメタル板等がある。なお、図1に示されるよう
に、電極基材3は固体高分子電解質膜1より小さい面積
のものが用いられ、電極触媒層2は電極基材3より小さ
い面積のものが用いられる。
Here, those which can be used as the solid polymer electrolyte membrane 1 have a sulfonic acid group as an ion exchange group.
An ionic solid polymer electrolyte membrane , for example, EI Dupont de Num
ours & Co) to Nafion
Or a sulfonated perfluorocarbon membrane sold under the trade name of Dow Chemical
l Co. There are similar membranes available from). In addition, what can be used as the electrode catalyst layer 2 includes a dispersion of platinum black fine particles and a polytetrafluoroethylene resin, and a solution obtained by hydrolyzing a solid polymer electrolyte membrane and dissolving in a solvent containing isopropyl alcohol as a main component. Then 50μ
m or a thin film sheet prepared using a high surface area carbon powder carrying platinum fine particles instead of platinum black fine particles, or directly electrolessly plated on the solid polymer electrolyte membrane 1. Platinum particle layer or platinum particles physically attached to the solid polymer electrolyte membrane 1. Further, examples of the material usable as the electrode substrate 3 include porous carbon paper and an expanded metal plate made of platinum plated titanium. In addition, as shown in FIG.
The electrode substrate 3 has an area smaller than the solid polymer electrolyte membrane 1.
The electrode catalyst layer 2 is smaller than the electrode base material 3.
Those with a large area are used.

【0013】つぎにホットプレスの条件について説明す
る。まず、ホットプレス時の一般的温度および圧力条件
について説明する。固体高分子電解質膜1は一般に13
0℃以上の温度で軟化し、210℃以上の温度で熱分解
を開始する。したがって、ホットプレスの温度は130
℃以上で210℃未満の温度が望ましい。また、固体高
分子電解質膜1は130℃以上の温度では10kgf/
cm2 以上の面圧で容易に変形する。したがって、ホッ
トプレスの圧力は10kgf/cm2 以上となる。な
お、電極基材3として前記カーボンペーパを使用する場
合には、カーボンの繊維が100kgf/cm2 以上の
面圧では切断されるおそれがあるため、ホットプレスの
最高圧力は100kg/cm2 未満が好ましいが、電極
基材3として前記エキスパンドメタル板を使用する場合
はこのような制限はない。
Next, the conditions for hot pressing will be described. First, general temperature and pressure conditions during hot pressing will be described. The solid polymer electrolyte membrane 1 generally has 13
Softens at a temperature of 0 ° C. or more and starts thermal decomposition at a temperature of 210 ° C. or more. Therefore, the temperature of the hot press is 130
A temperature of not less than 210 ° C and not less than 210 ° C is desirable. The solid polymer electrolyte membrane 1 has a pressure of 10 kgf /
Deforms easily with surface pressure of 2 cm2 or more. Therefore, the pressure of the hot press is 10 kgf / cm 2 or more. In the case of using the carbon paper as the electrode substrate 3, because there is a possibility that carbon fiber is cut at 100 kgf / cm 2 or more surface pressure, the maximum pressure of the hot pressing is less than 100 kg / cm 2 Although preferred, when the expanded metal plate is used as the electrode substrate 3, there is no such limitation.

【0014】つぎに、ホットプレス時の電極基材3の表
面の固体高分子電解質膜1に対する食い込み深さについ
て具体例を挙げて説明する。なお、この場合、固体高分
子電解質膜1としてナフィオン117を使用した。電極
基材3として厚さ0.1mmの前記カーボンペーパを使
用し、温度170℃、圧力50kgf/cm2 の条件で
ホットプレスして、カーボンペーパの食い込み深さが7
0μmに達している場合は、ホットプレスしてできたこ
の固体高分子電解質型電極4を水中で2昼夜放置して
も、固体高分子電解質膜1が膨張してカーボンペーパに
外れや脱落が生じることはなく、かつ、固体高分子電解
質型電極4の電気化学デバイスとしての機能も維持され
ている。
Next, the depth of penetration of the surface of the electrode substrate 3 into the solid polymer electrolyte membrane 1 during hot pressing will be described with reference to specific examples. In this case, Nafion 117 was used as the solid polymer electrolyte membrane 1. The carbon paper having a thickness of 0.1 mm was used as the electrode base material 3 and hot-pressed under the conditions of a temperature of 170 ° C. and a pressure of 50 kgf / cm 2 so that the carbon paper had a penetration depth of 7 mm.
When the thickness reaches 0 μm, even if the solid polymer electrolyte type electrode 4 formed by hot pressing is left in water for two days and nights, the solid polymer electrolyte membrane 1 expands and detaches or falls off the carbon paper. In addition, the function of the solid polymer electrolyte electrode 4 as an electrochemical device is maintained.

【0015】また、電極基材3として前記エキスパンド
メタル板を使用すると、同一温度・圧力で上記の場合よ
りさらに食い込み深さを大きくすることができるが、温
度を下げてエキスパンドメタル板をホットプレスにより
30μm以上食い込ませた場合、できた固体高分子電解
質型電極4はその固体高分子電解質膜1が吸湿した場合
でも、エキスパンドメタル板の外れや脱落はなく、か
つ、エキスパンドメタル板の電極基材3としての集電機
能に支障はなかった。
When the expanded metal plate is used as the electrode substrate 3, the bite depth can be further increased at the same temperature and pressure as compared with the above case. However, the temperature is lowered and the expanded metal plate is hot-pressed. When the solid polymer electrolyte type electrode 4 is bitten by 30 μm or more, even if the solid polymer electrolyte membrane 1 absorbs moisture, the expanded metal plate does not come off or fall off, and the expanded metal plate electrode substrate 3 There was no hindrance to the current collection function.

【0016】一方、電極基材3としてカーボンペーパと
エキスパンドメタル板のいずれを使用した場合でも、そ
の固体高分子電解質膜1への食い込み深さが30μm未
満の場合は、ホットプレス後、固体高分子電解質膜1が
吸湿して膨張すれば、電極基材3が固体高分子電解質膜
1から一部外れたり、脱落していまうおそれが強かっ
た。
On the other hand, regardless of whether carbon paper or expanded metal plate is used as the electrode substrate 3, if the penetration depth into the solid polymer electrolyte membrane 1 is less than 30 μm, the solid polymer If the electrolyte membrane 1 absorbs moisture and expands, there is a strong possibility that the electrode base material 3 may be partially removed from the solid polymer electrolyte membrane 1 or fall off.

【0017】その他種々の実験結果から、電極基材3の
固体高分子電解質膜1内への食い込み深さは、ホットプ
レス時の温度・圧力条件のみならず、電極触媒層2の組
成と厚さ、電極基材3の材質と形状、固体高分子電解質
膜1の種類等によっても変化することがわかったが、い
ずれにしても、吸湿による電極基材3の固体高分子電解
質膜1からの脱落を防止するために電極基材3の固体高
分子電解質膜1内への食い込み深さは30μm以上ある
ことが望ましいことがわかった。
From other various experimental results, the depth of penetration of the electrode substrate 3 into the solid polymer electrolyte membrane 1 depends not only on the temperature and pressure conditions during hot pressing, but also on the composition and thickness of the electrode catalyst layer 2. It was also found that the electrode base material 3 changed depending on the material and shape of the electrode base material 3, the type of the solid polymer electrolyte membrane 1, and the like. It has been found that it is desirable that the depth of penetration of the electrode substrate 3 into the solid polymer electrolyte membrane 1 be 30 μm or more in order to prevent the above.

【0018】つぎに上記条件でホットプレスし、電極基
材3が固体高分子電解質膜1内へ30μm以上食い込ん
でいる場合の電極触媒層2周りの状態について説明す
る。固体高分子電解質型電極4の電極触媒層2の断面を
走査形電子顕微鏡で観察すると、図2で示されるよう
に、電極触媒層2と固体高分子電解質膜1との反応界面
が3次元的に形成されていることがわかる。
Next, a state around the electrode catalyst layer 2 when the electrode base material 3 is hot pressed under the above conditions and the electrode base material 3 digs into the solid polymer electrolyte membrane 1 by 30 μm or more will be described. When the cross section of the electrode catalyst layer 2 of the solid polymer electrolyte type electrode 4 is observed with a scanning electron microscope, as shown in FIG. 2, the reaction interface between the electrode catalyst layer 2 and the solid polymer electrolyte membrane 1 is three-dimensional. It can be seen that they are formed in

【0019】すなわち、ホットプレス時に、固体高分子
電解質膜1が電極基材3の孔部内に入り込もうとする。
電極基材3の孔部内に侵入しようとする固体高分子電解
質膜1の動きにより、固体高分子電解質膜1と電極基材
3との間に配置された電極触媒層2は伸ばされて電極基
材3の孔部内に山形状またはポリープ状の突起(断面の
み見ると図2で示されるように蛇腹状に見える)となっ
て侵入する。同時に、固体高分子電解質膜1も電極基材
3の孔部内を電極触媒層2の突起の内面側まで入り込ん
でいて、電極触媒層2と固体高分子電解質膜1との反応
界面は3次元的に形成され、この反応界面は平面的なも
のに比べ拡大されている。したがって、この固体高分子
電解質型電極4では電極触媒層2の利用率を高めること
ができ、固体高分子電解質型電極4は小型で高性能な電
気化学デバイスとして利用される。
That is, at the time of hot pressing, the solid polymer electrolyte membrane 1 tries to enter the hole of the electrode substrate 3.
Due to the movement of the solid polymer electrolyte membrane 1 trying to penetrate into the hole of the electrode base material 3, the electrode catalyst layer 2 disposed between the solid polymer electrolyte membrane 1 and the electrode base material 3 is extended and The hole 3 of the material 3 penetrates as a mountain-shaped or polyp-shaped projection (only the cross section looks like a bellows shape as shown in FIG. 2). At the same time, the solid polymer electrolyte membrane 1 also penetrates into the hole of the electrode substrate 3 to the inner side of the protrusion of the electrode catalyst layer 2, and the reaction interface between the electrode catalyst layer 2 and the solid polymer electrolyte membrane 1 is three-dimensional. This reaction interface is enlarged compared to a planar one. Therefore, in the solid polymer electrolyte type electrode 4, the utilization rate of the electrode catalyst layer 2 can be increased, and the solid polymer electrolyte type electrode 4 is used as a small, high-performance electrochemical device.

【0020】実施例2.実施例1では温度が130℃か
ら210℃の条件下で電極基材3の表面を固体高分子電
解質膜1内に30μm以上の深さで食い込ませるように
ホットプレスしたが、この実施例2ではこの条件はその
まま守った状態で、電極基材3全体を固体高分子電解質
膜1内にすっぽり埋め込むように食い込ませた。このこ
とにより、電極基材3の固体高分子電解質膜1からの脱
落がより防止される。但し、この場合、両側の電極基材
3どうしが接触すれば電気化学デバイスとしての機能が
失われるため、この点は注意する必要がある。
Embodiment 2 FIG. In Example 1, hot pressing was performed so that the surface of the electrode substrate 3 was cut into the solid polymer electrolyte membrane 1 at a depth of 30 μm or more at a temperature of 130 ° C. to 210 ° C. While keeping these conditions as they were, the entire electrode substrate 3 was cut into the solid polymer electrolyte membrane 1 so as to be completely embedded therein. This further prevents the electrode substrate 3 from falling off from the solid polymer electrolyte membrane 1. However, in this case, if the electrode substrates 3 on both sides come into contact with each other, the function as an electrochemical device is lost.

【0021】なお、実施例1および実施例2では、固体
高分子電解質膜1の両面側に電極触媒層2と電極基材3
とを食い込ませる電気化学デバイスについて説明した
が、固体高分子電解質膜1の片面側にのみ電極触媒層2
と電極基材3とを食い込ませる電気化学デバイスに対し
てもこの発明は適用できる。
In Examples 1 and 2, the electrode catalyst layer 2 and the electrode base material 3 were provided on both sides of the solid polymer electrolyte membrane 1.
Has been described, but the electrode catalyst layer 2 is formed only on one side of the solid polymer electrolyte membrane 1.
The present invention can also be applied to an electrochemical device in which the electrode device 3 and the electrode substrate 3 bite.

【0022】[0022]

【発明の効果】以上の説明から明らかなようにこの発
よれば、電極触媒層を挟んでスルホン酸基をイオン交
換基としてもつイオン性の固体高分子電解質膜と、電極
触媒層より大きく、かつ、固体高分子電解質膜より小さ
い面積を有する電極基材とを130℃以上210℃未満
の温度下でホットプレスして、電極基材の表面を固体高
分子電解質膜内に30μm以上の深さまで食い込ませ
と供に、電極基材全体を固体高分子電解質膜内に食い込
ませたので、固体高分子電解質膜と電極触媒層との間に
3次元的な反応界面を形成できると供に、この反応界面
を特別な操作をすることなく維持できる。また、従来の
電気化学デバイスのように粗面化の工程が不要であり、
固体高分子電解質膜を用いた電気化学デバイスの製造作
業の容易化も図ることができる。
The inventions As is apparent from the above description, according to the present invention
According to the ionic solid polymer electrolyte membrane having a sulfonic acid group across the electrode catalyst layer as an ion-exchange group, electrode
Larger than the catalyst layer and smaller than the solid polymer electrolyte membrane
And hot pressing the electrode substrate having had the area at a temperature below 130 ° C. or higher 210 ° C., Ru was bite into the surface of the electrode substrate to 30μm or more depth to the solid polymer electrolyte in film
In addition, the entire electrode substrate is cut into the solid polymer electrolyte membrane.
Since Mase, the three-dimensional test the reaction interface can be formed between the solid polymer electrolyte membrane and the electrode catalyst layer can be maintained without the the reaction interface special operation. Also, it is a process of roughened to an electrochemical device of the traditional is unnecessary,
The manufacturing operation of the electrochemical device using the solid polymer electrolyte membrane can be facilitated.

【0023】[0023]

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

【図1】この発明の実施例1に関するホットプレス前の
固体高分子電解質型電極を構成する各部材の側面図であ
る。
FIG. 1 is a side view of members constituting a solid polymer electrolyte type electrode before hot pressing according to Embodiment 1 of the present invention.

【図2】この発明の実施例1に関する固体高分子電解質
型電極の側断面図である。
FIG. 2 is a side sectional view of a solid polymer electrolyte type electrode according to Embodiment 1 of the present invention.

【符号の説明】[Explanation of symbols]

1 固体高分子電解質膜 2 電極触媒層 3 電極基材 4 固体高分子電解質型電極(電気化学デバイス) DESCRIPTION OF SYMBOLS 1 Solid polymer electrolyte membrane 2 Electrode catalyst layer 3 Electrode substrate 4 Solid polymer electrolyte type electrode (electrochemical device)

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭58−126674(JP,A) 特開 昭62−196389(JP,A) 特開 昭58−126675(JP,A) (58)調査した分野(Int.Cl.7,DB名) H01M 8/00 - 8/24 ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-58-126774 (JP, A) JP-A-62-196389 (JP, A) JP-A-58-126675 (JP, A) (58) Field (Int.Cl. 7 , DB name) H01M 8/00-8/24

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 電極触媒層を挟んでスルホン酸基をイオ
ン交換基としてもつイオン性の固体高分子電解質膜と
前記電極触媒層より大きく、かつ、前記固体高分子電解
質膜より小さい面積を有する電極基材とを130℃以上
210℃未満の温度下でホットプレスして、前記電極基
材の表面を前記固体高分子電解質膜内に30μm以上の
深さまで食い込ませると供に、前記電極基材全体を前記
固体高分子電解質膜内に食い込ませたことを特徴とする
固体高分子電解質膜を用いた電気化学デバイスの製造方
法。
1. The method according to claim 1, wherein the sulfonic acid group is ion
An ionic solid polymer electrolyte membrane having an exchange group ,
Larger than the electrode catalyst layer, and the solid polymer electrolysis
An electrode substrate having an area less than Shitsumaku hot pressed at a temperature of lower than 130 ° C. or higher 210 ° C., Ru was bite into the surface of the electrode substrate to the solid polymer electrolyte 30μm or more depths in the membrane With the whole electrode substrate,
A method for manufacturing an electrochemical device using a solid polymer electrolyte membrane, characterized in that the electrochemical device is cut into a solid polymer electrolyte membrane.
JP04127484A 1992-05-20 1992-05-20 Method for manufacturing electrochemical device using solid polymer electrolyte membrane Expired - Fee Related JP3100754B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP04127484A JP3100754B2 (en) 1992-05-20 1992-05-20 Method for manufacturing electrochemical device using solid polymer electrolyte membrane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP04127484A JP3100754B2 (en) 1992-05-20 1992-05-20 Method for manufacturing electrochemical device using solid polymer electrolyte membrane

Publications (2)

Publication Number Publication Date
JPH05325983A JPH05325983A (en) 1993-12-10
JP3100754B2 true JP3100754B2 (en) 2000-10-23

Family

ID=14961086

Family Applications (1)

Application Number Title Priority Date Filing Date
JP04127484A Expired - Fee Related JP3100754B2 (en) 1992-05-20 1992-05-20 Method for manufacturing electrochemical device using solid polymer electrolyte membrane

Country Status (1)

Country Link
JP (1) JP3100754B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8373963B2 (en) 2010-01-26 2013-02-12 Akio Katano Ion/ozone wind generation device and method
US9620936B2 (en) 2013-05-13 2017-04-11 Katano Kogyo Co., Ltd. Ion/ozone wind generation device and method
KR20230006751A (en) 2021-07-04 2023-01-11 김철 Lifting type ionic wind air cleaner
KR20230006752A (en) 2021-07-04 2023-01-11 김철 Ionic wind type air cleaner

Families Citing this family (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1516311A (en) * 1998-06-16 2004-07-28 ���µ�����ҵ��ʽ���� polymer electrolyte fuel cell
US6599403B2 (en) * 1999-12-21 2003-07-29 Mitsubishi Denki Kabushiki Kaisha Electrochemical device using solid polymer electrolytic film
JP3604078B2 (en) * 2000-09-01 2004-12-22 本田技研工業株式会社 Electrode structure for fuel cell and manufacturing method thereof
JP3579886B2 (en) * 2000-09-01 2004-10-20 本田技研工業株式会社 Electrode structure for fuel cell and manufacturing method thereof
JP3579885B2 (en) * 2000-09-01 2004-10-20 本田技研工業株式会社 Electrode structure for fuel cell and manufacturing method thereof
JP4642656B2 (en) * 2003-02-18 2011-03-02 日本電気株式会社 Fuel cell electrode and fuel cell using the same
WO2004075322A1 (en) * 2003-02-18 2004-09-02 Nec Corporation Electrode for fuel cell, fuel cell and methods for manufacturing these
JP5252408B2 (en) * 2005-12-27 2013-07-31 日産自動車株式会社 High durability fuel cell
JP5082239B2 (en) * 2005-12-28 2012-11-28 大日本印刷株式会社 Catalyst layer-electrolyte membrane laminate and method for producing the same
JP5108240B2 (en) * 2006-03-20 2012-12-26 トヨタ自動車株式会社 Fuel cell and fuel cell manufacturing method
JP5184795B2 (en) 2006-06-06 2013-04-17 シャープ株式会社 FUEL CELL, FUEL CELL SYSTEM, AND ELECTRONIC DEVICE
WO2009017147A1 (en) 2007-08-02 2009-02-05 Sharp Kabushiki Kaisha Fuel cell stack and fuel cell system
WO2010114059A1 (en) 2009-04-01 2010-10-07 シャープ株式会社 Fuel cell stack and electronic apparatus provided with same
JP2010257669A (en) * 2009-04-23 2010-11-11 Toppan Printing Co Ltd Membrane electrode assembly, method for producing the same, and polymer electrolyte fuel cell

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8373963B2 (en) 2010-01-26 2013-02-12 Akio Katano Ion/ozone wind generation device and method
US9620936B2 (en) 2013-05-13 2017-04-11 Katano Kogyo Co., Ltd. Ion/ozone wind generation device and method
KR20230006751A (en) 2021-07-04 2023-01-11 김철 Lifting type ionic wind air cleaner
KR20230006752A (en) 2021-07-04 2023-01-11 김철 Ionic wind type air cleaner

Also Published As

Publication number Publication date
JPH05325983A (en) 1993-12-10

Similar Documents

Publication Publication Date Title
JP3100754B2 (en) Method for manufacturing electrochemical device using solid polymer electrolyte membrane
US5186877A (en) Process of preparing electrode for fuel cell
JP4699763B2 (en) One-step method for joining and sealing fuel cell membrane electrode assemblies
JP2013258143A (en) Enhanced catalyst interface for membrane electrode assembly
JPH07220742A (en) Solid polymer electrolyte fuel cell and method for producing electrode-ion exchange membrane assembly of the fuel cell
JPH08329962A (en) Polymer solid electrolyte membrane / electrode integrated molding and manufacturing method thereof
US10923736B2 (en) Method for producing fuel cell separator, and separator material
JPH06169583A (en) Reinforced thin-film electrode interface
US4992126A (en) Method for making a current collector bonded to a solid polymer membrane
CN115699373A (en) Method for manufacturing a membrane electrode assembly
EP2154744B1 (en) Process for producing solid polymer electrolyte membrane, and solid polymer electrolyte membrane
JPH07176317A (en) Method for manufacturing electrode / ion-exchange thin film assembly, and method for manufacturing electrode / ion-exchange thin film / electrode assembly
JPH0676838A (en) Ion exchange membrane fuel cell and its manufacture
CA2464326A1 (en) Electrolyte membrane/electrode union for fuel cell and process for producing the same
JPH07326363A (en) Ion conductivity imparting electrode and jointing material for electrode and electrolyte and cell using the ion conductivity imparting electrode
JPH1131515A (en) Polymer electrolyte membrane-gas diffusion electrode body and method for producing the same
JP2005108770A (en) Method for producing electrolyte membrane electrode assembly
JP2001085019A (en) Polymer electrolyte fuel cell and method for manufacturing electrode therefor
JP3555209B2 (en) Power generation layer of fuel cell and method of manufacturing the same
JP4824946B2 (en) Electrolyte membrane with protective film and production method thereof.
JP2003346839A (en) Composite thin film
JP2004119065A (en) Method for producing membrane electrode assembly of polymer electrolyte fuel cell
US20200321626A1 (en) Coaxial nanowire electrode
JP3097258B2 (en) Method for producing electrode for ion exchange membrane fuel cell
CA2610424A1 (en) Electrolyte membrane-electrode assembly and method for production thereof

Legal Events

Date Code Title Description
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20070818

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080818

Year of fee payment: 8

LAPS Cancellation because of no payment of annual fees