JPS58126675A - Ion exchange membrane fuel cell and its manufacture - Google Patents
Ion exchange membrane fuel cell and its manufactureInfo
- Publication number
- JPS58126675A JPS58126675A JP57008692A JP869282A JPS58126675A JP S58126675 A JPS58126675 A JP S58126675A JP 57008692 A JP57008692 A JP 57008692A JP 869282 A JP869282 A JP 869282A JP S58126675 A JPS58126675 A JP S58126675A
- Authority
- JP
- Japan
- Prior art keywords
- electrode
- exchange membrane
- ion exchange
- platinum
- nafion
- 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
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/1004—Fuel cells with solid electrolytes characterised by membrane-electrode assemblies [MEA]
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2300/00—Electrolytes
- H01M2300/0017—Non-aqueous electrolytes
- H01M2300/0065—Solid electrolytes
- H01M2300/0082—Organic polymers
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
Abstract
Description
【発明の詳細な説明】
本発明にイオン交換膜燃料’I池用II椿の構造、及び
その製造万I!22に関する。[Detailed Description of the Invention] The present invention provides the structure of the ion exchange membrane fuel 'II Camellia for I pond and its manufacture! Regarding 22.
イオン交換8Il燃料電池の代表的なものとして、水素
・aX燃料II池の構造を第1図に示す。燃料として電
槽へ流入して来る水素は負険上で分解さn1電子を放出
するととも罠、水素イオンを生成する。この水素イオン
はイオン交換pst通り正極へ達する。正極では水素イ
オン、電子、酸素か反応し水を虫取する。以上の反応に
於ける電子の負極から正極への移動が燃料III池外部
て取り出せる電流と成る訳である。FIG. 1 shows the structure of a hydrogen/aX fuel II pond, which is a typical ion exchange 8Il fuel cell. Hydrogen flowing into the battery tank as fuel is decomposed and releases n1 electrons, generating traps and hydrogen ions. These hydrogen ions reach the positive electrode through ion exchange pst. At the positive electrode, hydrogen ions, electrons, and oxygen react to remove water. The movement of electrons from the negative electrode to the positive electrode in the above reaction results in a current that can be taken out from the fuel III cell.
従来の1本的構造は電解質のイオン交換勝會両側から導
伝性の箔状または網状1憧ではさみ、プラス千ツクの外
枠で固足したものであった。こtらのII醜のweとし
て、電池の厚さが他の方式の電池と比較して薄くな9、
単位容積当り、あるいは率位重童当り、かなり高い出力
が得らnる点にある。The conventional one-piece structure was one in which the electrolyte ion exchange plate was sandwiched between conductive foil or mesh plates on both sides and secured with a plastic outer frame. The disadvantage of these II is that the battery is thinner than other types of batteries9.
It is at the point where a considerably high output can be obtained per unit volume or per unit weight.
しかし外枠で固足する次めに、網状電極とイオン交換膜
の接触が必ずしも均一に行なわnず、ま友機械的振動な
どにも弱い。しかも、外枠の厚みだけ薄型化に対する利
点が損なわnている。However, since the outer frame is fixed, the contact between the mesh electrode and the ion exchange membrane is not necessarily uniform, and it is also susceptible to mechanical vibrations. Moreover, the advantage of thinning is diminished by the thickness of the outer frame.
本発明はII極活物質であり、かつ集電体である金属製
の網状1iI陽をホットプレスにエフ、イオン交換編上
へ熱圧着することに工り一体化した。このことにエリ従
来のものと比較して、機械的衝激に対して吻めて強くな
ったため、信頼性が飛躍的に同上し友。しかも電池の?
]IiI化かより容易になった。また部品点数の減少に
エリ、組み立て性も非常に良くなつ之。In the present invention, a metal net-like 1iI positive material, which is the active material of the II electrode and a current collector, is integrated by hot pressing and bonding it onto an ion-exchange knitted fabric by thermocompression. In addition, compared to conventional products, it has become more resistant to mechanical shock, resulting in a dramatic increase in reliability. And what about batteries?
]IiI has become easier. In addition, the number of parts is reduced, and ease of assembly is greatly improved.
以下1本発明の実施例會水素・酸素燃料電池について説
明する。A hydrogen/oxygen fuel cell according to an embodiment of the present invention will be described below.
イオン交換膜としてナフィオン(デュポン社の登録商標
)倉用い、こnKl倫活物質と集1体を兼ねた白金網(
1180)2枚を両側へ密層させろ。そしてホットプレ
ス中、200℃でaOK4/dの圧力を5分間加える。Nafion (registered trademark of DuPont) was used as the ion exchange membrane, and platinum wire mesh (which also served as a collector for the active material) was used as the ion exchange membrane.
1180) Place the two sheets in close layers on both sides. Then, during hot pressing, a pressure of aOK4/d is applied at 200° C. for 5 minutes.
この操作によ・ジ白金製の網は熱にエリ軟化しtナフィ
オン中へ半ば埋め込1nる。この結果、白金襄の網がナ
フィオンに食い込むことにエリ、機械的振動などに4j
めて強くなつ之。このイオン交amと*憧の一体化さn
^ものの断面図を第2図に示す。By this operation, the diplatinum mesh is softened by the heat and is partially embedded into the Nafion. As a result, the net of platinum was cut into Nafion, and the mechanical vibration caused 4j.
I'm getting stronger. This ion interaction and the unification of longing
^A cross-sectional view of the object is shown in Figure 2.
このイオン交換膜と電極の一体物を図1で示し次と同様
の罐槽内に入n使用し九ところ、燃料電池の出力か外部
からの機械的振動に対しても安定に取り出せる工うKな
った。こnに電極とイオン交換mt−一体化したことに
LD、その密着性が半永久的と反った次めである。tf
C部品A数が減ったばかりでなく、組み立ての際、密層
性を良くするためのイオン交換膜、W極、外枠の位置の
調整確認を不要なものとでき次。This integrated ion-exchange membrane and electrode is shown in Figure 1, and when used in a container similar to the one shown below, it was found that the output of the fuel cell could be stably extracted even against external mechanical vibrations. became. Now that the electrode and ion exchange mt are integrated, the adhesion of the LD is semi-permanent and warped. tf
Not only has the number of parts A and C been reduced, but during assembly, it is no longer necessary to check and adjust the positions of the ion exchange membrane, W pole, and outer frame to improve layer density.
尚、W*に用いる金属製の網は白金以外にも、水素極(
負極)としてニッケルやパラジウム、酸素!!!(正極
)として銀やラネー・ニッケルなトを用いることができ
る。In addition to platinum, the metal mesh used for W* can also be used for hydrogen electrodes (
Nickel, palladium, and oxygen as negative electrodes! ! ! Silver or Raney nickel can be used as the positive electrode.
w41図は水素・@累イオン交換膜燃料1池の漁場横取
を示した断面図である。
1・・・水嵩の入口
2・・・酸素の入口
3・・・カスケラト
4・・・電槽板
5・・・イオン交換膜
6・・・11極
7・・・ガス室
8・・・ガス箇たは水の出口
第2図は本発明によるIN伽とイオン交換膜の一体物1
1−第1図と同じ方向から見た断面□である。
1・・・金属製のl14状電極
2・・・陽イオン交換膜
以 上
出願人 株式会社諏訪精工令
代理人 弁理士最上 務
OΦ
第2図Figure w41 is a cross-sectional view showing fishing ground capture for one pond of hydrogen/ion exchange membrane fuel. 1...Water volume inlet 2...Oxygen inlet 3...Cascellato 4...Battery plate 5...Ion exchange membrane 6...11 pole 7...Gas chamber 8...Gas Figure 2 shows an integrated structure of an IN cable and an ion exchange membrane according to the present invention.
1-This is a cross section □ seen from the same direction as in Figure 1. 1...Metallic L14-shaped electrode 2...Cation exchange membrane or above Applicant Suwa Seiko Co., Ltd. Agent Tsutomu Mogami OΦ Figure 2
Claims (2)
の網状11I極がイオン交換膜と一体であること管特命
とするイオン交換膜燃料電池用’I極。(1) I-electrode for ion-exchange membrane fuel cells in which the metallic net-like 11 I-electrode, which is the active material for the I-electrode and the current collector, is integrated with the ion-exchange membrane.
にエフ熱圧着しイオン交換膜燃料電池用II極とするこ
とt%書とするイオン交換膜燃料11池用電椿の製造方
法。(2) A method for producing a camellia for ion exchange membrane fuel 11 cell, in which a metal mesh is bonded to the cation exchange 11 using a hot press to make the electrode II for an ion exchange membrane fuel cell.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57008692A JPS58126675A (en) | 1982-01-22 | 1982-01-22 | Ion exchange membrane fuel cell and its manufacture |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57008692A JPS58126675A (en) | 1982-01-22 | 1982-01-22 | Ion exchange membrane fuel cell and its manufacture |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS58126675A true JPS58126675A (en) | 1983-07-28 |
Family
ID=11699967
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57008692A Pending JPS58126675A (en) | 1982-01-22 | 1982-01-22 | Ion exchange membrane fuel cell and its manufacture |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58126675A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0562747A2 (en) * | 1992-03-12 | 1993-09-29 | Mitsubishi Denki Kabushiki Kaisha | Oxygen concentration or humidity controlling apparatus |
NL9500253A (en) * | 1995-02-10 | 1996-09-02 | Stichting Energie | Method for wetting fuel gases as well as solid polymer fuel cell. |
JP2007123043A (en) * | 2005-10-27 | 2007-05-17 | Canon Inc | Solid-polymer fuel cell, catalyst layer thereof, manufacturing method thereof |
KR100847493B1 (en) | 2006-11-08 | 2008-07-22 | 한국전자통신연구원 | Method for Preparing Polymer Actuators with High Stability and Polymer Actuators Prepared by the Method |
JP2012178360A (en) * | 2012-05-11 | 2012-09-13 | Canon Inc | Catalyst layer of polymer electrolyte fuel cell, and polymer electrolyte fuel cell |
JP2012243430A (en) * | 2011-05-17 | 2012-12-10 | Toyota Motor Corp | Fuel cell and method for manufacturing fuel cell |
-
1982
- 1982-01-22 JP JP57008692A patent/JPS58126675A/en active Pending
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0562747A2 (en) * | 1992-03-12 | 1993-09-29 | Mitsubishi Denki Kabushiki Kaisha | Oxygen concentration or humidity controlling apparatus |
EP0562747A3 (en) * | 1992-03-12 | 1994-12-07 | Mitsubishi Electric Corp | Oxygen concentration or humidity controlling apparatus |
NL9500253A (en) * | 1995-02-10 | 1996-09-02 | Stichting Energie | Method for wetting fuel gases as well as solid polymer fuel cell. |
JP2007123043A (en) * | 2005-10-27 | 2007-05-17 | Canon Inc | Solid-polymer fuel cell, catalyst layer thereof, manufacturing method thereof |
KR100847493B1 (en) | 2006-11-08 | 2008-07-22 | 한국전자통신연구원 | Method for Preparing Polymer Actuators with High Stability and Polymer Actuators Prepared by the Method |
JP2012243430A (en) * | 2011-05-17 | 2012-12-10 | Toyota Motor Corp | Fuel cell and method for manufacturing fuel cell |
JP2012178360A (en) * | 2012-05-11 | 2012-09-13 | Canon Inc | Catalyst layer of polymer electrolyte fuel cell, and polymer electrolyte fuel cell |
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