JPS58150278A - Gas-separating plate for fuel cell - Google Patents
Gas-separating plate for fuel cellInfo
- Publication number
- JPS58150278A JPS58150278A JP57032834A JP3283482A JPS58150278A JP S58150278 A JPS58150278 A JP S58150278A JP 57032834 A JP57032834 A JP 57032834A JP 3283482 A JP3283482 A JP 3283482A JP S58150278 A JPS58150278 A JP S58150278A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- reaction
- separation plate
- fuel cell
- gas supply
- 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
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0223—Composites
- H01M8/0228—Composites in the form of layered or coated products
-
- 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
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0204—Non-porous and characterised by the material
-
- 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
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0213—Gas-impermeable carbon-containing materials
-
- 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)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Composite Materials (AREA)
- Fuel Cell (AREA)
Abstract
Description
【発明の詳細な説明】
本発明はりん酸などの酸性電解液を用いるマトリックス
型燃料電池のカーボン製ガス分離板に係り、分離板の反
応ガス供給溝に特殊な表面処理を施して反応ガスの供給
を円滑にするものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a carbon gas separation plate for a matrix fuel cell using an acidic electrolyte such as phosphoric acid. It facilitates supply.
単位セル(1)間に介在するガス分離板(2)は、一般
にグラファイトとバインダー(フェノール系樹脂)との
混合粉末をホットプレス後前記バインダーを高温熱処理
により炭化1〜で得られる本ので、その表裏両面には、
夫々反応ガスとしての空気及び水素ガスの各供給溝(3
1+41を有し、これら両ガスの分離体及び単位セル間
の接続導体として働く。The gas separation plate (2) interposed between the unit cells (1) is generally obtained by hot pressing a mixed powder of graphite and a binder (phenolic resin) and then carbonizing the binder by high temperature heat treatment. On both the front and back sides,
Each supply groove (3
1+41, and serves as a separator for both gases and a connecting conductor between the unit cells.
各反応ガスはこれら供給溝+31+41 e通って夫々
空気極(5)及び水素極f61 K拡散し、この拡散し
たガスは電解質マトリックス(7)を介して電気化学的
反応を起す。Each reaction gas passes through these supply grooves +31+41e and diffuses into the air electrode (5) and hydrogen electrode f61K, respectively, and this diffused gas causes an electrochemical reaction via the electrolyte matrix (7).
しかし分離板の表面はかなり↑給水性があり、その上各
供給溝+3+ +41の断面は巾が1.5〜2.Off
、高さが11’ll程度と極めて小さいので、電池反応
により生成した水特にこの生成水にマ) IJ 、クス
から溶出した高濃度のりん酸電解液が分離板(2)の供
給溝f31 +41に付着する。前者の生成水は電池作
動温度によって短時間で蒸発除去されるが俊者のりん酸
を含んだ水は蒸発し難いので、これが液滴となって供給
溝+3+ 141を塞ぎ、この溝への反応ガスの供給が
円滑に行なわれず、電極反応が不均一となり、電池劣化
の一因となっていた。However, the surface of the separation plate has a considerable water supply property, and the cross section of each supply groove +3+ +41 has a width of 1.5 to 2. Off
Since the height is extremely small at about 11'll, the water generated by the battery reaction, especially this generated water, is absorbed by the high concentration phosphoric acid electrolyte eluted from the gas into the supply groove f31 +41 of the separation plate (2). Attach to. The former generated water is evaporated and removed in a short time depending on the battery operating temperature, but water containing phosphoric acid is difficult to evaporate, so it forms droplets and blocks the supply groove +3+ 141, causing a reaction to this groove. Gas supply was not carried out smoothly, resulting in uneven electrode reactions and contributing to battery deterioration.
本発明はか\る反応ガス供給溝の目づまりを解消するも
ので、その特徴とする所は、反応ガス供給溝の表面に、
カーボンに比して水に濡れやすい親水性(水に対する接
触角が小さい)物質の被膜を形成することにより、分離
板の溝に付着した電解質を含む水を溝表面に拡散させて
液滴となるのを防止し、且被膜上に拡散した液を蒸発除
去させて反応ガスの供給を円滑にする点にある。The present invention eliminates the clogging of the reaction gas supply groove, and is characterized by the fact that on the surface of the reaction gas supply groove,
By forming a film of a hydrophilic material (lower contact angle with water) that is more easily wetted by water than carbon, water containing electrolyte adhering to the grooves of the separation plate is diffused onto the groove surface and becomes droplets. The purpose of this method is to prevent this, and to evaporate and remove the liquid that has spread onto the coating, thereby facilitating the supply of the reaction gas.
こ′>に云う親水性物質としては、カーボンに比し、水
に濡れやすいことは勿論、耐酸性、耐熱性を有する仁と
が必要で、例えば酸化アルミニウム(Aj?zOa)、
二酸化ケイ素(Si02)、酸化チタン(TiO2)な
どが挙げられる。The hydrophilic substance mentioned above must not only be more easily wetted by water than carbon, but also have acid resistance and heat resistance, such as aluminum oxide (Aj?zOa),
Examples include silicon dioxide (Si02) and titanium oxide (TiO2).
前記被膜の形成法としては、溝の表面に直接酸化物を付
着させる方法と、溝の表面に金属を蒸着させた後これを
酸化はせる方法とがあり、前者にHすI、[火炎溶射法
(fi’lame 5prayi、ng ) と化学
蒸着法(Va、por Plating )がある。There are two methods for forming the film: one is to deposit an oxide directly on the surface of the groove, and the other is to deposit metal on the surface of the groove and then oxidize it. There are two methods: chemical vapor deposition (Va, por plating) and chemical vapor deposition (Va, por plating).
火器溶射法は被膜材の粉末又は棒状体を酸素アセチレン
紅などで溝表面に焼きつける方法であり、化学的蒸着法
は気相反応法とも云い揮発性化合物を高温でのガス反応
・水素還元を利用して溝表面に薄膜を析出させる方法で
ある。Firearm spraying is a method in which powder or rod-shaped coating materials are baked onto the groove surface with oxygen acetylene red, etc., and chemical vapor deposition is also called a gas phase reaction method, which uses gas reaction and hydrogen reduction of volatile compounds at high temperatures. This method deposits a thin film on the groove surface.
本発明の実施例として、酸化アルミニウムを化学蒸着法
によってガス分離板(2)の溝+31 +41にコーテ
ングする場合を説明すれば、塩化アルミニウムの高温で
の熱分解と炭酸ガス及び水素ガスの導入により、次式
%式%
の反応によりAe2XO3の被膜+3+’t41’
を形成する。As an embodiment of the present invention, the case where aluminum oxide is coated on the grooves +31 to +41 of the gas separation plate (2) by chemical vapor deposition is explained. , Ae2XO3 film +3+'t41' by the reaction of the following formula % formula %
form.
被膜の厚みは10μ程度とした。The thickness of the coating was approximately 10 μm.
このように処理したガス分離板(2)の電極(5+ +
61との接触面に付着した被膜は機械的に削り落すか、
電極との接触面に被膜がつかないよう予めテープなどで
マスキングを施してもよい。The electrode (5+ +
Either mechanically scrape off the coating that adheres to the contact surface with 61, or
Masking may be performed in advance with tape or the like to prevent a film from adhering to the contact surface with the electrode.
上述の如く本発明によるカーボン製ガス分離板は、その
反応ガス供給溝が親水性物質の薄い被膜で覆われている
ので、分離板表面のJ佑水性に起Hして供給溝が電解液
を含んだ液滴によって目づまりを起すことがなくなり、
供給溝に付着した前記液は親水性被膜を拡散して液滴に
生成することなく蒸発除去される。As mentioned above, in the carbon gas separation plate according to the present invention, the reaction gas supply grooves are covered with a thin film of a hydrophilic substance, so that the supply grooves absorb the electrolyte due to the hydrophilicity on the surface of the separation plate. No more clogging caused by the contained droplets,
The liquid adhering to the supply groove diffuses through the hydrophilic coating and is evaporated and removed without forming droplets.
従って各供給溝へ反応ガスが円滑且均−に送られ電池特
性の向上と寿命の改善を図ることができる。Therefore, the reaction gas is sent smoothly and evenly to each supply groove, thereby improving battery characteristics and life.
第1図は本発明ガス分離板を備える電池スタックの一部
を破断して示す斜面図、@2図は同上の要部拡大断面図
である。
1・・・単位セル、2・・・ガス分離板、5.4・・・
反応ガス供給溝、6′、4′・・・被膜、5.6・・・
電極、7・・・電解質マトリックス。
出願人 三洋電機株式会社
代理人 弁理士 佐 野 静 夫1
3 675FIG. 1 is a partially cutaway perspective view of a battery stack equipped with a gas separation plate of the present invention, and FIG. 2 is an enlarged sectional view of the same essential parts. 1... Unit cell, 2... Gas separation plate, 5.4...
Reaction gas supply groove, 6', 4'... coating, 5.6...
Electrode, 7... electrolyte matrix. Applicant Sanyo Electric Co., Ltd. Agent Patent Attorney Shizuo Sano 1 3 675
Claims (3)
に、親水性物質よりなる被膜を形成したことを特徴とす
る燃料電池のガス分離板(1) A gas separation plate for a fuel cell, characterized in that a film made of a hydrophilic substance is formed on the surface of the reaction gas supply groove of the carbon gas separation plate.
、酸化チタンからなる群より選ばれたことを特徴とする
特許請求の範囲第1項記載の燃料電池のガス分離板(2) A gas separation plate for a fuel cell according to claim 1, wherein the hydrophilic substance is selected from the group consisting of aluminum oxide, silicon oxide, and titanium oxide.
する特許請求の範囲第1項記載の燃料電池のガス分離板(3) A gas separation plate for a fuel cell according to claim 1, wherein the coating has a thickness of about 10 μm.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57032834A JPS58150278A (en) | 1982-03-01 | 1982-03-01 | Gas-separating plate for fuel cell |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57032834A JPS58150278A (en) | 1982-03-01 | 1982-03-01 | Gas-separating plate for fuel cell |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS58150278A true JPS58150278A (en) | 1983-09-06 |
Family
ID=12369844
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57032834A Pending JPS58150278A (en) | 1982-03-01 | 1982-03-01 | Gas-separating plate for fuel cell |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58150278A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62186471A (en) * | 1986-02-12 | 1987-08-14 | Mitsubishi Electric Corp | Internally reformed type fuel cell |
JPH08138692A (en) * | 1994-11-04 | 1996-05-31 | Toyota Motor Corp | Fuel cell |
JP2001093539A (en) * | 1999-09-28 | 2001-04-06 | Matsushita Electric Ind Co Ltd | Solid polimer electrolytic fuel cell |
WO2001061775A3 (en) * | 2000-02-17 | 2002-08-22 | Nedstack Holding B V | Water removal in pem fuel cells |
-
1982
- 1982-03-01 JP JP57032834A patent/JPS58150278A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62186471A (en) * | 1986-02-12 | 1987-08-14 | Mitsubishi Electric Corp | Internally reformed type fuel cell |
JPH08138692A (en) * | 1994-11-04 | 1996-05-31 | Toyota Motor Corp | Fuel cell |
JP2001093539A (en) * | 1999-09-28 | 2001-04-06 | Matsushita Electric Ind Co Ltd | Solid polimer electrolytic fuel cell |
WO2001061775A3 (en) * | 2000-02-17 | 2002-08-22 | Nedstack Holding B V | Water removal in pem fuel cells |
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