JPS58163173A - Electrode for fuel cell - Google Patents
Electrode for fuel cellInfo
- Publication number
- JPS58163173A JPS58163173A JP57047920A JP4792082A JPS58163173A JP S58163173 A JPS58163173 A JP S58163173A JP 57047920 A JP57047920 A JP 57047920A JP 4792082 A JP4792082 A JP 4792082A JP S58163173 A JPS58163173 A JP S58163173A
- Authority
- JP
- Japan
- Prior art keywords
- catalytic layer
- layer
- base material
- carbon fiber
- water
- 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
- 239000000446 fuel Substances 0.000 title claims abstract description 11
- 239000003792 electrolyte Substances 0.000 claims abstract description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 21
- 239000007800 oxidant agent Substances 0.000 claims abstract description 4
- 239000005871 repellent Substances 0.000 claims description 7
- 238000000926 separation method Methods 0.000 claims description 2
- 239000000463 material Substances 0.000 abstract description 20
- 229920000049 Carbon (fiber) Polymers 0.000 abstract description 15
- 239000004917 carbon fiber Substances 0.000 abstract description 15
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 abstract description 15
- 238000006243 chemical reaction Methods 0.000 abstract description 14
- 230000003197 catalytic effect Effects 0.000 abstract 10
- 238000006555 catalytic reaction Methods 0.000 abstract 1
- 239000003054 catalyst Substances 0.000 description 22
- 238000000034 method Methods 0.000 description 6
- 239000011248 coating agent Substances 0.000 description 4
- 238000000576 coating method Methods 0.000 description 4
- 239000004615 ingredient Substances 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 2
- 230000002940 repellent Effects 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- -1 polytetrafluoroethylene Polymers 0.000 description 1
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 1
- 239000004810 polytetrafluoroethylene Substances 0.000 description 1
- 239000010970 precious metal Substances 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for 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
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Inert Electrodes (AREA)
Abstract
Description
【発明の詳細な説明】 この発明は燃料電池の電極構造に関するものである。[Detailed description of the invention] This invention relates to an electrode structure for a fuel cell.
従来この種の電極として第1図に示すものがあった。図
において、(1)はカーボン繊維基材、(2)は撥水層
、(3)は触媒層、(4)は親水層であり、これら(1
)〜(4)はt極(至)を構成している。そして、との
電1Monは第2図に示すように組まれて燃料電池の最
小単位を構成する。第2図において、(5)は電解質層
、(6)[1対のバイポーラ板、(7)はバイポーラ板
に設けられたガス流路である。A conventional electrode of this type is shown in FIG. In the figure, (1) is a carbon fiber base material, (2) is a water-repellent layer, (3) is a catalyst layer, and (4) is a hydrophilic layer.
) to (4) constitute the t-pole (to). The electric cells 1Mon are assembled as shown in FIG. 2 to constitute the minimum unit of a fuel cell. In FIG. 2, (5) is an electrolyte layer, (6) is a pair of bipolar plates, and (7) is a gas flow path provided in the bipolar plates.
次に動作について説明する。上下、それぞれのガス流路
(7)から供給された燃料および酸化剤は、多孔質のt
極Q[)のカーボン繊維基材(1)および撥水層(2)
中を拡散し、触媒層(3)に達する。触媒層(3)中の
電解質との界面(反応界面)でガスは触媒の作用でイオ
ン化する。親水層(4)は電解質を含浸させた非電子導
電性の多孔質部材よシなる電解質層(5)の電解質とな
じみをよくシ、触媒層(3)に反応界面をつくる。この
ようにして触媒層(3)の間は電解質でつながシ、一対
の電極間に電位を発生させる。Next, the operation will be explained. The fuel and oxidizer supplied from the upper and lower gas channels (7) are fed through the porous t
Carbon fiber base material (1) and water-repellent layer (2) of Kyoku Q [)
It diffuses inside and reaches the catalyst layer (3). At the interface with the electrolyte (reaction interface) in the catalyst layer (3), the gas is ionized by the action of the catalyst. The hydrophilic layer (4) is compatible with the electrolyte of the electrolyte layer (5), which is a non-electronically conductive porous member impregnated with an electrolyte, and forms a reaction interface in the catalyst layer (3). In this way, the catalyst layers (3) are connected by the electrolyte, and a potential is generated between the pair of electrodes.
バイポーラ板(6)は電解質層(5)と一対の電極01
をはさんで支持し、ガスの供給と集電の働らきをする。The bipolar plate (6) has an electrolyte layer (5) and a pair of electrodes 01
It is supported between the two, and functions to supply gas and collect current.
従来の電極α1は上記のように構成されているので、各
層ごとに成分を変えてスプレー法や漏逸法で基材に塗布
せねばならなか゛りた。また特性を発揮するのに反応界
面(電解質とガスの界面)が触媒層中に到達し、゛かつ
撥水j−へずれ込まないことが必要で、十分な特性が出
るまで一定の時間がかかることと反応界面が触媒層を通
過してしまうと特性が落ち寿命がなくなってしまうとい
う欠点があった。Since the conventional electrode α1 is constructed as described above, it is no longer necessary to change the ingredients for each layer and apply it to the base material by a spray method or a leakage method. In addition, in order to exhibit the characteristics, the reaction interface (the interface between the electrolyte and the gas) must reach the catalyst layer and not slip into the water repellent layer, so it takes a certain amount of time to exhibit sufficient characteristics. Another disadvantage is that if the reaction interface passes through the catalyst layer, the properties deteriorate and the life span is shortened.
この発明は上記のような従来のものの欠点を除去する為
になされたもので、電極をカーボン繊維基材と触媒層に
よ多構成し、カーボン繊維基材に強い撥水性を与え、触
媒j−にはカーボン繊維基材側から電解質側に向かって
撥水性が弱くなるような勾配を持たせることに↓シ、十
分な特性がでるまでの時間を短縮しかつ寿命を延ばすこ
とができる電極を提供することを目的としている。This invention was made in order to eliminate the drawbacks of the conventional ones as described above.The electrode is composed of a carbon fiber base material and a catalyst layer, and the carbon fiber base material has strong water repellency. By creating a gradient in which the water repellency decreases from the carbon fiber base material side to the electrolyte side, we provide an electrode that can shorten the time it takes to develop sufficient properties and extend its life. It is intended to.
以下、この発明の一実施例を図について説明する。第3
図において、α刀は残漬水処理をしたカーボン繊維基材
、(2)はカーボン繊維基材0刀側から電解質層に向け
て撥水性が徐々に弱くなっている触媒層であり、これら
α漫、(2)は電極−を構成する。An embodiment of the present invention will be described below with reference to the drawings. Third
In the figure, α is a carbon fiber base material treated with residual water, and (2) is a catalyst layer whose water repellency gradually weakens from the zero side of the carbon fiber base toward the electrolyte layer. (2) constitutes an electrode.
この撥水力に勾配を持った触媒層(6)の製造法の一例
について述べる。触に層(2)は一定量の貴金属、1
触媒を炭素粉末に担持させたものとポリテトラフル
オロエチレンとの混合液をカーボン繊維基材(ロ)上に
スプレー法や漏過法で塗布する。触媒層(6)の厚さは
150〜200μmで上記方法で塗布する場合、数度に
わたって塗布が行われる。各回の塗布ごとに300°C
前後の温度で加熱焼成してやる。この時、撥水性は温度
を高くする程、また保持時間を長くする程強くなり、一
定の温度で処理を繰返しても。An example of a method for manufacturing the catalyst layer (6) having a gradient in water repellency will be described. The layer (2) contains a certain amount of precious metal, 1
A mixed solution of a catalyst supported on carbon powder and polytetrafluoroethylene is applied onto the carbon fiber base material (b) by a spray method or a leakage method. The thickness of the catalyst layer (6) is 150 to 200 μm, and when it is coated by the above method, it is coated several times. 300°C for each application
It is heated and fired at different temperatures. At this time, the higher the temperature and the longer the holding time, the stronger the water repellency becomes, even if the treatment is repeated at a constant temperature.
温度を徐々に低くして処理をしても目的の撥水カーの勾
配が得られる。Even if the treatment is carried out by gradually lowering the temperature, the desired gradient of the water-repellent car can be obtained.
次に動作について説明する。上下、それぞれのガス流路
(7)から供給された燃料および酸化剤は、多孔質の電
極−のカーボン繊維基材α刀および触媒層(6)を拡散
し、触媒N1I(2)中の電解質との界面(反応界面)
でガスは触媒の作用でイオン化する。Next, the operation will be explained. The fuel and oxidizer supplied from the upper and lower gas channels (7) diffuse through the carbon fiber base material of the porous electrode and the catalyst layer (6), and the electrolyte in the catalyst N1I (2). interface with (reaction interface)
The gas is ionized by the action of a catalyst.
触媒層(2)の電解質J@ (5)と接する側の撥水性
は十分弱くなっているので電解質とよくなじみすばやく
触媒層(2)中に反応界面を形成する。触媒層@内部は
順次強い撥水性が持たせであるので容易に移動せずに安
定して触媒層(2)中に反応界面を形成している。Since the water repellency of the side of the catalyst layer (2) in contact with the electrolyte J@ (5) is sufficiently weak, it blends well with the electrolyte and quickly forms a reaction interface in the catalyst layer (2). Since the inside of the catalyst layer (2) has strong water repellency, it does not move easily and forms a stable reaction interface in the catalyst layer (2).
電極勾)の間は、上記のように電解質で継ながシ、一対
の電極間に電位を発生する。The electrode gradient is connected by an electrolyte as described above, and a potential is generated between the pair of electrodes.
このように上記実施例によれば一種の触媒層成分でtW
iの撥水性の程度を変えているので、新水層や撥水層を
わざわざ塗布する必要がなくなシ、したがって、成分を
変えた塗布材料が一種類ですみ、材料に対応した塗布装
置も1機で
なお上記実施例では、カーボン繊維基材(ロ)に残漬水
性を持たせたが、必しも必要でない。また、触Kl−(
2)には電解質(5]との接触側で撥水性を弱くカーボ
ン繊維基材側0刀で強くなるように勾配をつけているが
その中間層に最も強い撥水性を与えてもよい。さらに上
記実施例では撥水性の強度調整を熱処理によって行なっ
たが、トリテトラフルオロエチレンの濃度を変えること
によって行なってもよい。In this way, according to the above embodiment, one type of catalyst layer component can achieve tW
Since the degree of water repellency of i is changed, there is no need to take the trouble of applying a new water layer or water repellent layer.Therefore, only one type of coating material with different ingredients is needed, and coating equipment compatible with the material can be used. In the above example, the carbon fiber base material (b) was made to have residual aqueous properties, but this is not always necessary. Also, touch Kl-(
2) has a gradient so that the water repellency is weak on the side in contact with the electrolyte (5) and strong on the carbon fiber base side, but the strongest water repellency may be given to the intermediate layer. In the above examples, the strength of water repellency was adjusted by heat treatment, but it may also be done by changing the concentration of tritetrafluoroethylene.
以上のように、この発明によれば電解質層なはさむ両電
極の撥水性能に勾配を持たせたことにより、特性が出る
までの時間が短縮され、使用中は、反応界面が移動して
もよシ長く触媒層中に反応界面を固定するのでよシ安定
で長い寿命の電極の提供が可能となる。As described above, according to the present invention, by creating a gradient in the water repellency of both electrodes sandwiching the electrolyte layer, the time required for properties to appear is shortened, and even if the reaction interface moves during use, Since the reaction interface is fixed in the catalyst layer for a longer period of time, it is possible to provide a more stable and long-life electrode.
また、親水層や撥水層をわざわざ作らないので、厚みを
その分だけ薄くすることも可能となり、不用な層の電気
抵抗がなくなシ出力ロスを減すことが可能である。Furthermore, since a hydrophilic layer or a water-repellent layer is not specially created, the thickness can be reduced by that amount, and the electrical resistance of unnecessary layers is eliminated, making it possible to reduce output loss.
第1図は従来の電極構造の一例を示す断面図、第2図は
第1図における電極が組込まれた燃料電池の構成を示す
断面図、第3図はこの発明の一実施例によるxiの構造
を示す断面図、第4図は第3図における電極を適用した
燃料電池の構成を示す断面図である。
図において、(5)は電解質層、(6)はガス分離板。
αQは電極である。
尚、各図中同一符号は同一または相当部を示す。
代理人 葛野信−
第1図
第2図
/
第3図
手続補正書(ハ灸)
57715
昭和 年 月 日
2、発明の名称
燃料電池用電極
3、補正をする者
事件との関係 特許量1領人
住 所 東京都千代]]1区丸の内部丁目2番
3号名 称(601,) 三菱電機株式会社代表者
片由仁八部
4、代理人
住 所 東京都千代目1区丸の山王丁目2番3
−g=5、補正の対象
明細書堰発明の詳細な説明の欄
6、補正の内容
(1)明細書の第5頁第2行に「新水」とあるのを「親
水」に訂正する。
(2)同上の第5頁第4行ないし第5行に「成分を・・
・・・・も1機で」とあるのを「塗布材料の成分は1種
類ですみ、材料に対応した塗布装置も1機で目的の電極
を作ることができる。」に訂正する。
(3)同上の第5頁第6行に「基材(ロ)に」とあるの
を「基材(11)にも」に訂正する。
(4)同上の第5頁第12行に「トリテトラフルオロ」
とあるのを「ポリテトラフルオロ」に訂正する。FIG. 1 is a sectional view showing an example of a conventional electrode structure, FIG. 2 is a sectional view showing the structure of a fuel cell incorporating the electrode in FIG. 1, and FIG. 3 is a sectional view showing an example of a conventional electrode structure. FIG. 4 is a cross-sectional view showing the structure of a fuel cell to which the electrode in FIG. 3 is applied. In the figure, (5) is an electrolyte layer, and (6) is a gas separation plate. αQ is an electrode. Note that the same reference numerals in each figure indicate the same or corresponding parts. Agent Makoto Kuzuno - Figure 1 Figure 2/Figure 3 Procedural Amendment (Ha Moxibustion) 57715 Showa Year, Month, Day 2, Name of the invention Fuel cell electrode 3, Relationship with the person making the amendment Patent amount 1 territory Address: 2-3, Marunouchi-chome, 1-ku, Tokyo Name (601,) Mitsubishi Electric Corporation Representative: Katayuni Hachibe 4, Agent Address: 2-2, Sanno-chome, Marunouchi-chome, Chiyo, 1-ku, Tokyo Number 3
-g=5, Specification subject to amendment Detailed explanation column 6 of the weir invention, Contents of amendment (1) In the second line of page 5 of the specification, "Shinsui" is corrected to "Shinui" . (2) On page 5, lines 4 and 5 of the same article, there is a statement that says, “Ingredients...
. . . with just one machine" should be corrected to "The coating material only requires one type of component, and the desired electrode can be made with one coating device compatible with the material." (3) On page 5, line 6 of the same document, the phrase "on the base material (b)" is corrected to "also on the base material (11)." (4) "Tritetrafluoro" on page 5, line 12 of the same
Correct that to "polytetrafluoro".
Claims (1)
、これをはさむ撥水性を有する2枚の電極と、これに燃
料および酸化剤を供給するガス分離板よ多構成されるも
のにおいて、上記両電極の撥水性能に勾配を持たせたこ
とを特徴とする燃料電池用電極。An electrolyte layer made of a non-conductive porous member impregnated with an electrolyte, two water-repellent electrodes sandwiching the electrolyte layer, and a gas separation plate that supplies fuel and an oxidizer to the electrolyte layer. A fuel cell electrode characterized in that both of the electrodes have a gradient in water repellency.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57047920A JPS58163173A (en) | 1982-03-23 | 1982-03-23 | Electrode for fuel cell |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57047920A JPS58163173A (en) | 1982-03-23 | 1982-03-23 | Electrode for fuel cell |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS58163173A true JPS58163173A (en) | 1983-09-27 |
Family
ID=12788798
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57047920A Pending JPS58163173A (en) | 1982-03-23 | 1982-03-23 | Electrode for fuel cell |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58163173A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60216457A (en) * | 1984-04-11 | 1985-10-29 | Hitachi Ltd | Fuel cell |
JPS61133567A (en) * | 1984-11-30 | 1986-06-20 | Shin Kobe Electric Mach Co Ltd | Manufacturing method of gas diffusion electrode for fuel cells |
JPS61288376A (en) * | 1985-06-14 | 1986-12-18 | Hitachi Ltd | Method for manufacturing electrode plates for fuel cells |
JPS6210865A (en) * | 1985-07-05 | 1987-01-19 | Mitsubishi Electric Corp | Electrode-matrix bonding body for fuel cell and its manufacture |
JP2001015145A (en) * | 1999-06-25 | 2001-01-19 | Sanyo Electric Co Ltd | Solid polyelectrolyte fuel cell |
JP2001357869A (en) * | 2000-06-14 | 2001-12-26 | Sanyo Electric Co Ltd | Solid high-polymer type fuel cell stack |
CN111082069A (en) * | 2019-12-20 | 2020-04-28 | 大连博融新材料有限公司 | Implanted gradient composite electrode, production method and application thereof |
-
1982
- 1982-03-23 JP JP57047920A patent/JPS58163173A/en active Pending
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60216457A (en) * | 1984-04-11 | 1985-10-29 | Hitachi Ltd | Fuel cell |
JPS61133567A (en) * | 1984-11-30 | 1986-06-20 | Shin Kobe Electric Mach Co Ltd | Manufacturing method of gas diffusion electrode for fuel cells |
JPS61288376A (en) * | 1985-06-14 | 1986-12-18 | Hitachi Ltd | Method for manufacturing electrode plates for fuel cells |
JPS6210865A (en) * | 1985-07-05 | 1987-01-19 | Mitsubishi Electric Corp | Electrode-matrix bonding body for fuel cell and its manufacture |
JP2001015145A (en) * | 1999-06-25 | 2001-01-19 | Sanyo Electric Co Ltd | Solid polyelectrolyte fuel cell |
JP2001357869A (en) * | 2000-06-14 | 2001-12-26 | Sanyo Electric Co Ltd | Solid high-polymer type fuel cell stack |
CN111082069A (en) * | 2019-12-20 | 2020-04-28 | 大连博融新材料有限公司 | Implanted gradient composite electrode, production method and application thereof |
CN111082069B (en) * | 2019-12-20 | 2022-07-29 | 大连博融新材料有限公司 | Implanted gradient composite electrode, production method and application thereof |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4038463A (en) | Electrode reservoir for a fuel cell | |
DE69800361D1 (en) | Gas diffusion electrodes for polymer electrolyte fuel cells | |
JP2009123703A (en) | Fuel cell including plurality of unit cells connected in series by current collector | |
JPS58163173A (en) | Electrode for fuel cell | |
CA2098606C (en) | Efficiency enhancement for solid-electrolyte fuel cell | |
TW200406080A (en) | Process for the preparation of a solid oxide fuel cell | |
US4031291A (en) | Hydrogen-oxidizing catalyst, and fuel cell electrode using same | |
JPH065289A (en) | Polymer electrolyte fuel cell | |
ATE267464T1 (en) | METHOD FOR PRODUCING ELECTRODES, COMPONENTS, HALF-CELLS AND CELLS FOR ELECTROCHMIC ENERGY CONVERTERS | |
JP2002208415A (en) | Fuel cell containing solid electrolyte layer | |
JPH08106915A (en) | Solid polymer fuel cell electrode and method of manufacturing fuel cell | |
JPS5975568A (en) | Fuel cell | |
JPS58115770A (en) | Fuel cell | |
JPH08138715A (en) | Polymer electrolyte fuel cell and method of manufacturing the same | |
KR102752319B1 (en) | Metal separator and method for manufacturing the same | |
JPH07262997A (en) | Electrode base for fuel cell | |
JPS57124864A (en) | Gas diffusion electrode of fuel cell | |
JP3706624B2 (en) | Fuel cell system | |
KR200334723Y1 (en) | Compression jig for manufacturing unit cell of polymer electrolyte fuel cell | |
JPH06103982A (en) | Fuel cell | |
JPS5763776A (en) | Fuel cell | |
KR20250039264A (en) | Metal separator and method for manufacturing the same | |
JP2002075404A (en) | Solid oxide fuel cell and power generation method thereof | |
JP4561086B2 (en) | Method for producing electrode for fuel cell | |
JP2883342B2 (en) | Method of impregnating catalyst layer with electrolyte solution |