JPS5943649Y2 - gas diffusion electrode - Google Patents

gas diffusion electrode

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Publication number
JPS5943649Y2
JPS5943649Y2 JP1978052750U JP5275078U JPS5943649Y2 JP S5943649 Y2 JPS5943649 Y2 JP S5943649Y2 JP 1978052750 U JP1978052750 U JP 1978052750U JP 5275078 U JP5275078 U JP 5275078U JP S5943649 Y2 JPS5943649 Y2 JP S5943649Y2
Authority
JP
Japan
Prior art keywords
electrode
gas
current collector
gas diffusion
metal current
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
Application number
JP1978052750U
Other languages
Japanese (ja)
Other versions
JPS54156145U (en
Inventor
和雄 小関
亨彦 鶴岡
Original Assignee
富士電機株式会社
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 富士電機株式会社 filed Critical 富士電機株式会社
Priority to JP1978052750U priority Critical patent/JPS5943649Y2/en
Publication of JPS54156145U publication Critical patent/JPS54156145U/ja
Application granted granted Critical
Publication of JPS5943649Y2 publication Critical patent/JPS5943649Y2/en
Expired 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

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  • Inert Electrodes (AREA)

Description

【考案の詳細な説明】 本考案は、外部から燃料と酸素(もしくは空気)とを連
続的に供給して、電気化学的に反応させて電気エネルギ
を取出す燃料電池におけるガス拡散電極に関する。
[Detailed Description of the Invention] The present invention relates to a gas diffusion electrode in a fuel cell in which fuel and oxygen (or air) are continuously supplied from the outside and are electrochemically reacted to extract electrical energy.

第1図は水素−酸素燃料電池の原理説明図である。FIG. 1 is a diagram explaining the principle of a hydrogen-oxygen fuel cell.

図において水素電極2および酸素電極3の向きあう面に
よって、電解液室1が形成され、水素電極2の他の面に
は、水素ガス室4、酸素電極3の他の面には酸素ガス室
5が設けられている。
In the figure, an electrolyte chamber 1 is formed by the opposing surfaces of the hydrogen electrode 2 and the oxygen electrode 3, a hydrogen gas chamber 4 is formed on the other surface of the hydrogen electrode 2, and an oxygen gas chamber is formed on the other surface of the oxygen electrode 3. 5 is provided.

6は水素電極2訟よび酸素電極3に接続される負荷であ
る。
6 is a load connected to the hydrogen electrode 2 and the oxygen electrode 3.

電解液室1内の電解液には苛性カリのようなアルカリ性
水溶液昔たは硫酸のような酸性水溶液がある。
The electrolyte in the electrolyte chamber 1 includes an alkaline aqueous solution such as caustic potash or an acidic aqueous solution such as sulfuric acid.

水素電極2および酸素電極3は、多孔性金属、活性炭な
どを基材とし、白金、パラジウムなどを触媒とし、さら
にポリ4弗化エチレン(商品名テフロン)、ポリエチレ
ンなどを結着剤として使用し、焼結して、多数の細孔を
有する厚さ約O15閣ないし0.8van程度の薄板に
昔とめられる。
The hydrogen electrode 2 and the oxygen electrode 3 are made of porous metal, activated carbon, etc. as a base material, platinum, palladium, etc. as a catalyst, and polytetrafluoroethylene (trade name: Teflon), polyethylene, etc. as a binder. It was sintered and fastened into a thin plate with many pores about 0.15 to 0.8 van in thickness.

なお、これらの電極2,3は結着剤の量を加減して、電
解液がガス側へ洩れるのを防ぐ撥水層と、電解液が浸透
してぬれている親水層と、との撥水層と親水層との中間
に存在する触媒層とから形成されている。
In addition, these electrodes 2 and 3 adjust the amount of binder to create a repellent layer between the water-repellent layer that prevents the electrolyte from leaking to the gas side and the hydrophilic layer that is wetted by the electrolyte. It is formed from a catalyst layer existing between an aqueous layer and a hydrophilic layer.

一般に単電池の出力電圧は約IV出力電流密度は数百m
lv’c4程度であるから、所要の電圧、電流を得るた
めには、この単電池を複数個積層してブロックとし、さ
らにそのブロックを接続しテ燃料電池が構成される。
Generally, the output voltage of a single cell is approximately IV, and the output current density is several hundred m
Since the voltage is about lv'c4, in order to obtain the required voltage and current, a plurality of these single cells are stacked to form a block, and the blocks are further connected to form a fuel cell.

しかして、電極で発生した電気は、できるだけ簡単な方
法で、かつ効率よく集電されることが必要である。
Therefore, the electricity generated by the electrodes needs to be collected as simply and efficiently as possible.

このために、突起部を有する導電性の集電板をガス側の
電極面に圧着して集電する方法が知られている。
For this purpose, a method is known in which a conductive current collector plate having protrusions is pressure-bonded to the gas-side electrode surface to collect current.

この方法によれば、単電池を積層する際に、この単電池
を積重ねるだけで内部で直列に接続することができる。
According to this method, when stacking unit cells, it is possible to internally connect them in series simply by stacking the unit cells.

しかし、電極2゜3のガス室側の面は、撥水性を高める
ために、撥水剤としてポリ4弗化エチレンが多量に用い
られたり、多孔性の弗化樹脂シートを密着せしめること
もある。
However, in order to improve water repellency, a large amount of polytetrafluoroethylene is used as a water repellent, or a porous fluoride resin sheet is sometimes attached to the surface of the electrode 2゜3 on the gas chamber side. .

このために、この面の電気的抵抗が著しく高くなり、こ
の面に集電板を圧着しても集電が十分に得られず、さら
に、電極2,3のガス室4.5側の面に、表面に突起部
を有する集電板が直接接触するから、電極2,3面の被
圧着部分のガスの拡散が悪くなり、電極性能が低下する
という問題があった。
For this reason, the electrical resistance of this surface becomes extremely high, and even if a current collector plate is crimped to this surface, sufficient current collection cannot be obtained. Furthermore, since the current collector plates having protrusions on their surfaces are in direct contact with each other, there is a problem in that gas diffusion in the press-bonded portions of the electrodes 2 and 3 is poor, resulting in a decrease in electrode performance.

このために、内部にち−ける直列接続による集電方法を
採用することができず、電極2,3にそれぞれ集電端子
を設け、単電池の外部に取出して直列接続するから、そ
の構成が複雑化するという欠点があった。
For this reason, it is not possible to adopt a current collection method using a series connection inside the cell, and the electrodes 2 and 3 are each provided with a current collection terminal, which is taken out to the outside of the cell and connected in series. The drawback was that it was complicated.

本考案は、上述の点に鑑み、従来技術の欠点を除き集電
板による集電効果が向上し、構成が簡易化し、かつ集電
板と電極との間のガスの拡散が十分に得られ、電極性能
を長期に亘り維持し得るガス拡散電極を提供することを
目的とする。
In view of the above points, the present invention eliminates the drawbacks of the conventional technology, improves the current collection effect by the current collector plate, simplifies the configuration, and achieves sufficient gas diffusion between the current collector plate and the electrode. The object of the present invention is to provide a gas diffusion electrode that can maintain electrode performance over a long period of time.

このような目的は本考案によれば、電極と、この電極を
介して互に接するガス室と電解液室とを有する単電池を
複数個積層して形成される燃料電池用のガス拡散電極で
あって、前記電極と一体的に構成され、前記ガス室側に
折返された折返し部を有する網目状の金属製集電部材と
、前記ガス室に設けられ、表面に突起部を有し、前記突
起部により前記金属製集電部材の折返し部に圧着し集電
された金属製集電板とを備え、前記電極と金属製集電板
との間に、前記金属製集電部材の折返し部を介在し、ガ
スが拡散される隙間が構成されることにより達成される
According to the present invention, this purpose is achieved by a gas diffusion electrode for fuel cells formed by stacking a plurality of unit cells each having an electrode and a gas chamber and an electrolyte chamber that are in contact with each other through the electrode. a mesh-like metal current collecting member configured integrally with the electrode and having a folded part folded back toward the gas chamber; a metal current collector plate that is crimped to the folded part of the metal current collector member by a protrusion and collects current; the folded part of the metal current collector member is provided between the electrode and the metal current collector plate; This is achieved by creating a gap through which the gas is diffused.

次に、本考案の実施例を図面に基づき、詳細に説明する
Next, embodiments of the present invention will be described in detail based on the drawings.

第2図は本考案の実施例の概略構成図を示し、Aはその
正面図、Bはその側面図、第3図は第2図の使用状態に
おける概略構成図である。
FIG. 2 shows a schematic configuration diagram of an embodiment of the present invention, A is a front view thereof, B is a side view thereof, and FIG. 3 is a schematic diagram of the configuration in the usage state shown in FIG. 2.

第2図において短形状の金属製集電部材、本実施例では
金網11は電極7の集電材であり、かつ補強材である。
In FIG. 2, a rectangular metal current collecting member, in this embodiment a wire mesh 11, is a current collecting material for the electrode 7 and also serves as a reinforcing material.

この金網11の中央部の一面には、ガス側層である撥水
層8、他面には触媒層・親水層9からなる正方形状の電
極部10が一体的に焼結される。
A square electrode portion 10 consisting of a water-repellent layer 8 serving as a gas side layer and a catalyst layer/hydrophilic layer 9 on the other side is integrally sintered on one side of the central portion of the wire mesh 11.

この金網11の上部および下部は、第2図のようにガス
側層80面に折返されて、ガス側層のほぼ全面に折返し
部12を形成する。
The upper and lower parts of this wire mesh 11 are folded back to the gas side layer 80 surface, as shown in FIG. 2, to form a folded part 12 on almost the entire surface of the gas side layer.

この折返し部12ば、本実施例では電極部10のほぼ全
面に設けられているが、これに限るものではなく、部分
的に折返し部を形成することも可能である。
Although the folded portion 12 is provided on almost the entire surface of the electrode portion 10 in this embodiment, the folded portion 12 is not limited to this, and it is also possible to form the folded portion partially.

次に、第4図は第3図における本考案の実施例による燃
料電池の概略構成図を示す。
Next, FIG. 4 shows a schematic diagram of the fuel cell according to the embodiment of the present invention shown in FIG.

図にち・いて第1図および第3図と同一の機能を有する
部分には、同一の符号が付されている。
In the figures, parts having the same functions as those in FIGS. 1 and 3 are given the same reference numerals.

13は突起部を有する金属製集電板、14は電極7を支
持するセル枠、15は燃料電池の両端部のセル枠、16
は燃料電池の両端部の集電板13に接続された集電端子
である。
13 is a metal current collector plate having protrusions, 14 is a cell frame that supports the electrode 7, 15 is a cell frame at both ends of the fuel cell, 16
are current collecting terminals connected to current collecting plates 13 at both ends of the fuel cell.

これらの複数個の電極7は、複数個のセル枠14.15
と共に、複数個の電解溶室1と、水素ガス室4および酸
素ガス室5とを形成し各ガス室4,5には電極7に圧着
して集電する複数個の集電板13が介在し、積層構造形
燃料電池を構成する。
These plurality of electrodes 7 are connected to a plurality of cell frames 14 and 15.
Together, a plurality of electrolysis chambers 1, a hydrogen gas chamber 4, and an oxygen gas chamber 5 are formed, and each gas chamber 4, 5 is interposed with a plurality of current collector plates 13 that are crimped to the electrodes 7 to collect current. and constitute a stacked structure fuel cell.

上述の構成による本考案の機能を説明する。The functions of the present invention having the above-mentioned configuration will be explained.

導電性を有する金属製集電板13は、この集電板13の
両面に形成された突起部によって、電極7の金網製の折
返し部12に圧着し集電する。
The electrically conductive metal current collector plate 13 is crimped to the metal mesh folded part 12 of the electrode 7 by projections formed on both sides of the current collector plate 13 to collect current.

従って、この燃料電池は、複数個の電極7を、それぞれ
直列に接続するための集電端子の必要がなく、複数個の
単電池を積み重ねるのみで、内部で直列に接続される。
Therefore, this fuel cell does not require current collecting terminals for connecting the plurality of electrodes 7 in series, and can be internally connected in series by simply stacking a plurality of unit cells.

なお、本実施例は、集電板13が直接に電極7のガス側
層に密着することなく、電極7との間に金網製の折返し
部12が介在するために、集電板13の突起部と電極7
との間に隙間が構成される。
Note that in this embodiment, the current collector plate 13 does not directly contact the gas side layer of the electrode 7, but the folded part 12 made of wire mesh is interposed between the current collector plate 13 and the electrode 7, so that the protrusion of the current collector plate 13 part and electrode 7
A gap is created between the two.

従って、電極7の表面におけるガスの拡散が阻害される
ことがない。
Therefore, the diffusion of gas on the surface of the electrode 7 is not inhibited.

次に、第5図は本考案の他の実施例の概略構成図、第6
図は第5図の使用状態における概略構成図を示す。
Next, FIG. 5 is a schematic configuration diagram of another embodiment of the present invention, and FIG.
The figure shows a schematic diagram of the configuration in the usage state of FIG. 5.

第5図において電極17には正方形状の金網18の中央
部に、正方形状の電極部19が一体的に焼結される。
In FIG. 5, in the electrode 17, a square electrode portion 19 is integrally sintered at the center of a square wire mesh 18.

この金網18の4個所の角は第6図のように折返されて
、電極部19のガス側層のほぼ全面に折返し部20を形
成する。
The four corners of the wire mesh 18 are folded back as shown in FIG. 6 to form a folded part 20 on almost the entire surface of the gas side layer of the electrode part 19.

この電極17は第4図における電極7と同様に、集電板
13およびセル枠14.15と共に、内部で直列に接続
されて燃料電池を構成する。
Similar to the electrode 7 in FIG. 4, this electrode 17 is internally connected in series with the current collecting plate 13 and the cell frame 14, 15 to constitute a fuel cell.

なお、この折返し部20は、本実施例では電極部19の
ほぼ全面に設けられているがこれに限るものではなく、
部分的に折返し部を形成することも可能である。
Although the folded portion 20 is provided on almost the entire surface of the electrode portion 19 in this embodiment, the folded portion 20 is not limited to this.
It is also possible to form a partially folded portion.

以上説明するように本考案によれば、電極の補強材およ
び集電材としての金網をガス側層面に折返して折返し部
を形威し、この折返し部に突起部を有する集電板を圧着
するため、特別な集電接続を用いることなく集電効果が
向上し、(2)集電板の突起がガス拡散電極の撥水層面
に直接接触せず、その間に網目状の金網が介在するので
、電極面のガス拡散が阻害されないという効果を奏する
As explained above, according to the present invention, a wire mesh serving as an electrode reinforcing material and a current collector is folded back to the gas side layer surface to form a folded part, and a current collecting plate having a protrusion is crimped onto this folded part. , the current collection effect is improved without using a special current collection connection, and (2) the protrusions of the current collection plate do not come into direct contact with the water-repellent layer surface of the gas diffusion electrode, and a wire mesh is interposed between them. This has the effect that gas diffusion on the electrode surface is not inhibited.

なお、網目状の金属製集電部材は、本実施例では金網で
あるが、これに限るものでなく、エキスバンドメタルな
どを通用することができる。
Note that although the mesh-like metal current collecting member is a wire mesh in this embodiment, it is not limited to this, and an expanded metal or the like may be used.

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

第1図は燃料電池の原理説明図、第2図は本考案の実施
例の概略構成図を示し、Aはその正面図、Bはその側面
図、第3図は第2図の使用状態における概略構成図、第
4図は第3図における本考案の実施例による燃料電池の
概略構成図、第5図は本考案の他の実施例の概略構成図
、第6図は第5図の使用状態における概略構成図である
。 7.17・・・・・・電極、10.19・・・・・・電
極部、11.18・・・・・・金網、12.20・・・
・・・折返し部、13・・・・・・集電板、14.15
・・・・・・セル枠、16・・・・・・集電端子。
Fig. 1 is a diagram explaining the principle of a fuel cell, Fig. 2 is a schematic diagram of an embodiment of the present invention, A is a front view thereof, B is a side view thereof, and Fig. 3 is a diagram showing the state of use shown in Fig. 2. 4 is a schematic diagram of a fuel cell according to an embodiment of the present invention in FIG. 3; FIG. 5 is a schematic diagram of another embodiment of the present invention; FIG. 6 is a diagram showing the use of FIG. It is a schematic block diagram in a state. 7.17... Electrode, 10.19... Electrode part, 11.18... Wire mesh, 12.20...
... Folded part, 13... Current collector plate, 14.15
...Cell frame, 16...Current collector terminal.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 電極と、この電極を介して互に接するガス室と電解液室
とを有する単電池を複数個積層して形成される燃料電池
用のガス拡散電極であって、前記電極と一体的に構成さ
れ前記ガス室側に折返された折返し部を有する網目状の
金属製集電部材と、前記ガス室に設けられ表面に突起部
を有し前記突起部により前記金属製集電部材の折返し部
に圧着された金属製集電板とを備え、前記電極と金属製
集電板との間にガスが拡散される隙間が構成されたこと
を特徴とするガス拡散電極。
A gas diffusion electrode for a fuel cell formed by stacking a plurality of unit cells each having an electrode and a gas chamber and an electrolyte chamber in contact with each other via the electrode, the gas diffusion electrode being integrally formed with the electrode. a mesh-like metal current collecting member having a folded part folded back toward the gas chamber side; and a mesh-like metal current collecting member provided in the gas chamber and having a protrusion on its surface and crimped to the folded part of the metal current collecting member by the protrusion. What is claimed is: 1. A gas diffusion electrode comprising: a metal current collector plate made of metal, and a gap through which gas is diffused between the electrode and the metal current collector plate.
JP1978052750U 1978-04-22 1978-04-22 gas diffusion electrode Expired JPS5943649Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1978052750U JPS5943649Y2 (en) 1978-04-22 1978-04-22 gas diffusion electrode

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1978052750U JPS5943649Y2 (en) 1978-04-22 1978-04-22 gas diffusion electrode

Publications (2)

Publication Number Publication Date
JPS54156145U JPS54156145U (en) 1979-10-30
JPS5943649Y2 true JPS5943649Y2 (en) 1984-12-25

Family

ID=28944515

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1978052750U Expired JPS5943649Y2 (en) 1978-04-22 1978-04-22 gas diffusion electrode

Country Status (1)

Country Link
JP (1) JPS5943649Y2 (en)

Also Published As

Publication number Publication date
JPS54156145U (en) 1979-10-30

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