JPH01137565A - Fuel cell - Google Patents
Fuel cellInfo
- Publication number
- JPH01137565A JPH01137565A JP62295508A JP29550887A JPH01137565A JP H01137565 A JPH01137565 A JP H01137565A JP 62295508 A JP62295508 A JP 62295508A JP 29550887 A JP29550887 A JP 29550887A JP H01137565 A JPH01137565 A JP H01137565A
- Authority
- JP
- Japan
- Prior art keywords
- layer
- electrolyte
- fuel cell
- reservoir
- stored
- 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
- H01M8/0289—Means for holding the electrolyte
-
- 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
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04276—Arrangements for managing the electrolyte stream, e.g. heat exchange
- H01M8/04283—Supply means of electrolyte to or in matrix-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
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Fuel Cell (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
この発明は、積層形燃料電池のガス分離板に関するもの
である。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] This invention relates to a gas separation plate for a stacked fuel cell.
第4図は例えば特公昭58−152号公報に示された従
来の燃料電池の最も代表的なセル構成を示す断面図であ
る。図において、(1)は電解質を保持するマトリック
ス、(2)および(3)は電極であり、例えば炭素繊維
などで構成された多孔質の電極基材(4)(5)に電解
質を含む触媒層(6) (7)が設けられており、端部
には湿潤ガスシール部+81 (91が設けられている
。FIG. 4 is a cross-sectional view showing the most typical cell structure of a conventional fuel cell disclosed in, for example, Japanese Patent Publication No. 58-152. In the figure, (1) is a matrix that holds an electrolyte, (2) and (3) are electrodes, and catalysts containing electrolytes are placed in porous electrode base materials (4) and (5) made of carbon fiber, etc. The layers (6) (7) are provided, and the ends are provided with a wet gas seal +81 (91).
叫は不透気性の例えば緻密な炭素の板で形成されたガス
分離板(セパレータ又はインタコネクタとも呼ばれる〕
であり、その両面には燃料ガスおよび酸化剤ガスの流路
となる互いに直交する溝(13Q11が形成されている
。なお、一般的にはマトリックス(IJと電極(2+
(3)を組合せたもの(以下単位発電素子と称す〕とガ
ス分離板αGとを交互に積層して燃料電池が構成される
。A gas separation plate (also called a separator or interconnector) is made of an air-impermeable plate, such as dense carbon.
Grooves (13Q11) perpendicular to each other are formed on both sides of the grooves, which serve as flow paths for fuel gas and oxidant gas.In general, the matrix (IJ and electrodes (2+
A fuel cell is constructed by alternately stacking a combination of (3) (hereinafter referred to as a unit power generation element) and gas separation plates αG.
次に動作について説明する。ガス分離板αQの互いに直
交する溝Q3(ト)に、それぞれ燃料ガスおよび酸化剤
ガスを供給する。これらのガスは、電極基材(41(5
1中で拡散され電極(21(31の触媒層(6) (7
1の全面に達し、マトリックス(1)を通して反応し発
電する。Next, the operation will be explained. A fuel gas and an oxidizing gas are respectively supplied to mutually orthogonal grooves Q3 (g) of the gas separation plate αQ. These gases are applied to the electrode base material (41(5)
catalyst layer (6) (7
1, reacts through the matrix (1), and generates electricity.
ここで、反応に使われなかった余剰ガスおよび反応生成
物である水蒸気ガスは、溝cla(ト)を通じて外部に
排出されるが、この排出ガス中には、マトリックス(υ
および′rt極(21(3)に含まれる電解質が燃料電
池の動作条件で決まる蒸気となって存在し、電解質も外
部へ排出される。電極(21(3)の面内には反応の多
い部分と少ない部分が存在し、反応の多い部分では反応
生成物である水蒸気ガスや余剰ガスが多く、これらと共
に電解質も外部へ多く排出される。従って、長期間発電
していると反応の多い部分での電解質の社が少しづつ減
少し、最終的にはマトリックス(1)に反応に必要な量
の電解質がなくなり出力がでなくなる。この問題を解決
するために本出願人による特願昭61−168725号
では、ガス分離板の一部を多孔質にして、この多孔質の
部分に反応に直接関与しない余剰の電解質を貯蔵するこ
とが示されている。Here, surplus gas not used in the reaction and water vapor gas which is a reaction product are exhausted to the outside through the groove cla (g), but this exhaust gas contains a matrix (υ
The electrolyte contained in the electrode (21(3)) exists in the form of vapor determined by the operating conditions of the fuel cell, and the electrolyte is also discharged to the outside. There are parts where there are many reactions and parts where there are few reactions, and in the parts where there is a lot of reaction, there is a lot of water vapor gas and surplus gas which are reaction products, and a lot of electrolyte is also discharged to the outside along with these. The amount of electrolyte in the matrix (1) decreases little by little, and eventually there is no longer enough electrolyte in the matrix (1) for the reaction, and no output is produced.In order to solve this problem, the applicant filed a patent application filed in 1983. No. 168725 discloses that a part of the gas separation plate is made porous, and excess electrolyte not directly involved in the reaction is stored in this porous part.
なお、湿潤ガスシール+81 (91は、燃料ガスおよ
び酸化剤ガスが多孔質の電極基材(41(5)から外部
へ漏洩するのを防いでいる。Note that a wet gas seal +81 (91) prevents fuel gas and oxidant gas from leaking to the outside from the porous electrode base material (41 (5)).
従来の燃料電池は以上のように構成されているので、電
解質はマトリックス(1)、電極(21(30こしか保
持されておらず、長期の運転を行なった場合、蒸散・飛
散などにより電解質が不足し、電解質の補給を頻繁に行
なう必要があった。また、この問題を解決するためにな
された特願昭61−168725号においても、ガス分
離板の多孔質部に貯蔵した余剰の電解質がな(なってし
まうと、この多孔質部に電解質を補給する手段がないた
め、ガス分離板に多孔質部がないものと同様に補給を頻
繁に行なう必要が生ずるという問題点があった。Conventional fuel cells are constructed as described above, so only the matrix (1) and electrodes (21 (30) are retained, and when operated for a long period of time, the electrolyte is lost due to evaporation, scattering, etc.) There was a shortage of electrolyte, and it was necessary to frequently replenish the electrolyte.Also, in Japanese Patent Application No. 168725/1989, which was filed to solve this problem, excess electrolyte stored in the porous part of the gas separation plate was (If this happens, there is no means for replenishing the electrolyte into this porous portion, so there is a problem in that it is necessary to replenish the electrolyte as frequently as in the case where the gas separation plate does not have a porous portion.
この発明は上記のような問題点を解消するためになされ
たもので、ガス分離板に設けた多孔質部に電解質を常に
補給できる燃料電池を得ることを目的とする。This invention was made to solve the above-mentioned problems, and its object is to provide a fuel cell that can constantly replenish electrolyte to a porous portion provided in a gas separation plate.
この発明に係る燃料電池は、電解質を保持するマトリッ
クスとこれを挾む一対の電極とにより構成された単位発
電素子、一方の面に複数の溝を有し多孔質の第1層と、
この第1層の他方の面に一方の面が当接された不透気性
の第zlilと、この第2脂の他方の面に一方の面が当
接され他方の面に上記第1層の溝と直交する複数の溝を
有し多孔質の第3層と、この第3層および上記第1層の
端部に溝方向に添って設けられ上記第2層と一体化され
た不透気性のシール部とで構成され、上記単位発電素子
と交互に積層されるガス分離板、上記シール部に電解質
が貯溜される貯溜部を設けるとともに、この貯溜部を上
記第1層または第3層に連通させたものである。The fuel cell according to the present invention includes a unit power generation element composed of a matrix holding an electrolyte and a pair of electrodes sandwiching the matrix, a porous first layer having a plurality of grooves on one surface,
An impermeable zlil whose one surface is in contact with the other surface of this first layer, and one surface which is in contact with the other surface of this second layer and the other surface of the first layer is in contact with the other surface of the second layer. a porous third layer having a plurality of grooves orthogonal to the groove; and an air impermeable layer provided along the groove direction at the ends of the third layer and the first layer and integrated with the second layer. a gas separation plate which is stacked alternately with the unit power generating element; a storage part in which the electrolyte is stored is provided in the seal part; and the storage part is placed in the first layer or the third layer. It is a communication.
この発明における貯溜部は第1[または第3層に連通ず
ることにより、貯溜部内に貯溜される電解質を上記第1
wJまたは第3層に常に補給する。The reservoir in this invention communicates with the first [or third layer] so that the electrolyte stored in the reservoir can be transferred to the first layer.
Always replenish wJ or 3rd layer.
以下、この発明の一実施例を図について説明する。第1
図はこの発明の一実施例による燃料電池のセル構成を示
す分解斜視図、第2図は第1図のガス分離板の一部を示
す部分斜視図である。第1図および第2図において、(
1)から(3]は上記従来のものと同一のものであり、
単位発電素子を構成する。α旧よこの単位発電素子と交
互に積層されるガス分離板である。ガス分離板(6)に
おいて、口は一方の面に複数の湯口がリブ部Q4および
ウェブ部側により形成され多孔質の第1層、aSはこの
第111の他方の面すなわちウェブ部側と接着一体化さ
れた不透気性の第2層、靭は一方の面に溝(7)がリブ
邪曲およびウェブ部(4)により形成され多孔質の第3
層であり、溝(7)が第1層(6)のma3と直交する
向きに他方の面が第2層theに接着一体化されている
。An embodiment of the present invention will be described below with reference to the drawings. 1st
1 is an exploded perspective view showing the cell structure of a fuel cell according to an embodiment of the present invention, and FIG. 2 is a partial perspective view showing a part of the gas separation plate of FIG. 1. In Figures 1 and 2, (
1) to (3) are the same as the above conventional ones,
Constitutes a unit power generation element. This is a gas separation plate that is alternately stacked with unit power generation elements on both sides. In the gas separation plate (6), a plurality of sprues are formed on one surface by the rib portion Q4 and the web portion side, and the porous first layer aS is bonded to the other surface of this No. 111, that is, the web portion side. The integrated air-impermeable second layer has grooves (7) on one side formed by rib bends and web portions (4) and a porous third layer.
The other surface is adhesively integrated with the second layer the, with the groove (7) perpendicular to ma3 of the first layer (6).
ゆは第1層@の両端部に溝方向に添って設けられ第2層
QOと接着一体化された不透気性のシール部、(支)は
第3層σηの両端部に溝方向に添って設けられ第2層O
Qと接着一体化された不透気性のシール部、卿はシール
部局に端部が封止された溝状に形成された貯溜部であり
、第3mσηと連通する連通穴■および封止された端部
を貫通する貫通穴(7)が設けられている。(至)は貫
通穴(至)をふさぐ栓である。Yu is an air-impermeable seal part that is provided along the groove direction at both ends of the first layer @ and is adhesively integrated with the second layer QO. The second layer O
The air-impermeable sealing part that is integrated with Q is a reservoir formed in the shape of a groove whose end is sealed in the sealing part, and there is a communication hole that communicates with the third mση and a sealed part. A through hole (7) is provided through the end. (to) is a plug that closes the through hole (to).
なお、上記のように構成されたガス分離板口は複合化リ
ブ付セパレータとも呼ばれ、単位発電素子と交互に積層
されて燃料電池を構成するが、この時、第1/1H1a
および第3層σηに電解質が貯蔵されるとともに、貯溜
部(至)に電解質が貯溜される。The gas separation plate port configured as described above is also called a composite ribbed separator, and is stacked alternately with unit power generating elements to constitute a fuel cell.
The electrolyte is stored in the third layer ση, and the electrolyte is stored in the storage portion (to).
次に動作について説明する。ガス分離板συの第1層側
および第3層aηに形成された溝□□□および(7)に
それぞれ燃料ガスおよび酸化剤ガスを供給する。Next, the operation will be explained. Fuel gas and oxidizing gas are supplied to the grooves □□□ and (7) formed in the first layer side and the third layer aη of the gas separation plate συ, respectively.
この時、ガス分離板口の第2層はこれらの溝aaaaを
流れる燃料ガスと酸化剤ガスが互に混じるのを防いでお
り、両ガスは電極(21(3)へ達し、イオン化してマ
トリックス(1)を通して反応し発電が行なわれる。こ
こで、反応に使われなかった余剰ガスや反応生成物であ
る水蒸気ガスは、溝03(ト)を通じて外部へ排出され
るが、この排出ガス中には、マトリックス(1)や電極
+21 (31に含まれる電解質を蒸気として含み、電
解質が外部へ排出される。従って、長期の運転を行なっ
た場合には、マトリックス(υおよび電極(21(31
甲の電解質が不足してくるが、ガス分離板口の第1層(
ロ)および第3層側に貯蔵された電解質が、第11dQ
3および第3層側のウェブ部C15Gl)を浸透して自
由に第1層側および第3層0内を移動し、リブ部σ4Q
1を通して不足分を補ってマトリックス(1)および電
極(2) (31へ移動する。At this time, the second layer of the gas separation plate port prevents the fuel gas and oxidizing gas flowing through these grooves aaaa from mixing with each other, and both gases reach the electrode (21(3)), are ionized, and form a matrix. The reaction occurs through (1) and generates electricity. Here, surplus gas that is not used in the reaction and water vapor gas that is a reaction product are exhausted to the outside through groove 03 (g). contains the electrolyte contained in the matrix (1) and the electrode +21 (31) as vapor, and the electrolyte is discharged to the outside.
The electrolyte in the upper part becomes insufficient, but the first layer (
b) and the electrolyte stored on the third layer side is
3 and the web portion C15Gl) on the third layer side and freely move within the first layer side and the third layer 0, and the rib portion σ4Q
1 to make up for the shortage and move to matrix (1) and electrode (2) (31).
第3図は、電解質がリン酸の場合のリン酸蒸発量と運転
時間の関係を動作温度が205℃と220℃の場合につ
いて示したものであり、運転時間の累積が致方時間レベ
ルになると、電解質のセル内の貯蔵風を越える策になる
。しかも、動作温度が高くなると電解質の蒸発量も多く
なる。従って、高温で致方時間運転するためには、ガス
分離板(ロ)の内部に貯蔵する電解質の値を多くすると
ともに、外部から電解質を補給することが必要である。Figure 3 shows the relationship between the amount of phosphoric acid evaporated and the operating time when the electrolyte is phosphoric acid at operating temperatures of 205°C and 220°C. , it becomes a measure to overcome the storage wind inside the electrolyte cell. Moreover, as the operating temperature increases, the amount of electrolyte evaporation also increases. Therefore, in order to operate at high temperatures for as long as possible, it is necessary to increase the amount of electrolyte stored inside the gas separation plate (b) and to replenish the electrolyte from the outside.
ガス分離板αDのシール部(支)の貯溜部Qに貯溜され
た電解質は、連冗9穴(ロ)を通って第3層側へ移動し
、第31曽a力の電解質が少ない所、あるいは電解質の
濃度が小さい所へ浸透するとともに、第3m1lI力の
リブI’ Ql 8 i11+って電% tz+ (3
)およびマトリックス(1)へ移動する。シール部(資
)の貯溜部(至)に貯溜された電解質がこの移動によっ
て消費されなくなってしまうと、貫沖穴(イ)の栓(至
)を抜いて、外部から貫通穴(ハ)に電解質を注入し、
貯溜部(イ)に電解質を貯溜する。このようにして、致
方時間レベルの長期運転においても、シール部局の貯溜
部峙に電解質を貯溜および補給することができ、連通穴
(財)を通して第3層に常に補給することができるので
、安定に動作することができる。The electrolyte stored in the storage part Q of the seal part (support) of the gas separation plate αD moves to the third layer side through the nine consecutive holes (b), and the electrolyte of the 31st a force is small. Alternatively, as the electrolyte penetrates into a place where the concentration is small, the rib of the third m1lI force I' Ql 8 i11+ is electric% tz+ (3
) and move to matrix (1). When the electrolyte stored in the storage part (to) of the seal part (part) is no longer consumed by this movement, the plug (to) of the through-hole (a) is removed and the through-hole (c) is inserted from the outside. inject electrolytes,
Electrolyte is stored in the storage part (a). In this way, even during long-term operation, electrolyte can be stored and replenished in the storage section of the seal section, and the third layer can be constantly replenished through the communication hole. Can operate stably.
以上、電解質の蒸散・飛散等による不足分の補給機能を
説明したが、特に電解質がリン酸の場合などでは、起動
停止あるいは運転条件(動作圧力。Above, we have explained the function of replenishing the shortage due to electrolyte evaporation, scattering, etc., but especially when the electrolyte is phosphoric acid, it is necessary to change the starting/stopping or operating conditions (operating pressure).
動作温度、ガス利用率、セル面内位置等)によって電解
質の体積が太き(変化(膨張・収縮〕し、この電解質の
体積変化を吸収する機能も必要である。ガス分離板συ
の第1層(6)および第3層αηは、電解質を貯蔵【ノ
てはいるが、史に空孔部を残した状態になっており、運
転中に電解質マトリックスtl+や電極(2+ (31
で膨張したr!i解質を吸収できるとともに、電解質の
収縮の場合は、不足の場合と同じで必要な部分に電解質
は戻る。The volume of the electrolyte changes (expands and contracts) depending on the operating temperature, gas utilization rate, position within the cell plane, etc., and a function to absorb this volume change of the electrolyte is also required. Gas separation plate συ
The first layer (6) and the third layer αη store the electrolyte, but they are in a state where they leave voids, and during operation, the electrolyte matrix tl+ and the electrode (2+ (31
Inflated r! iSolytes can be absorbed, and in the case of electrolyte contraction, the electrolyte returns to the necessary part as in the case of a shortage.
なお、上記実施例では、シール部艶の貯溜部口に(川も
挿入さね、ていない場合について説明したが、第31−
〇力の気孔径と同じか、あるいは大きい気孔径を有する
多孔質体を貯溜部口に挿入して空間を充てんすると、貯
溜部Qの長手方向に対して電解質がより均一に分布し、
必要以上に@3層α力へ電解質が移動せず、第31シα
ηで不足した量の電解質のみを貯溜部[株]から補給す
ることができる。In addition, in the above embodiment, a case was explained in which the seal part gloss was not inserted into the reservoir opening.
〇If a porous body with a pore diameter equal to or larger than the pore diameter of the pores is inserted into the reservoir mouth to fill the space, the electrolyte will be distributed more uniformly in the longitudinal direction of the reservoir Q.
The electrolyte does not move to the 3rd layer α force more than necessary, and the 31st layer α
Only the amount of electrolyte lacking in η can be replenished from the reservoir.
ま1こ、上記実施例ではシール部口にのみ貯溜部−を設
けた場合について説明したが、貯溜部(至)はシール部
製のみ、あるいはシール部ゆ(資)の両方に設けてもよ
く、第1層側または第3鳩Uに連通しておれば、上記実
施例と同様の効果を突する。Also, in the above embodiment, the case where the reservoir is provided only at the mouth of the seal is explained, but the reservoir may be provided only in the seal, or in both the mouth of the seal. , if it communicates with the first layer side or the third dove U, the same effect as in the above embodiment can be achieved.
以上のように、この発明によれば燃料電池を、電解質を
保持するマトリックスとこれを挾む一対の電極とにより
構成された単位発電素子、一方の面に複数の溝を有し多
孔質の第1層と、この第1層の他方の面に一方の面が当
接された不透気性の第2層と、この第2層の他方の面に
一方の面が当接され他方の面に上記第1#の溝と直交す
る複数の溝を有し多孔質の第3層と、この第3層および
上記第17層の向@部に溝方向に添って設けられ上記第
2崖と一体化された不透気性のシール部とでa成され上
記単位発電素子と交互に積層されるガス分離板、上記シ
ール部に電解質が貯溜される貯溜部を設けるとともに、
この貯溜部が上記第1層または第3Mに連通するように
構成したので、第1層または第3層に貯溜部から常に電
解質を補給できるため、外部から電解質の補給を頻繁に
行なう必要なく長期の運転ができる燃料電池が得られる
効果がある。As described above, according to the present invention, a fuel cell includes a unit power generating element constituted by a matrix holding an electrolyte and a pair of electrodes sandwiching the matrix; one layer, an air-impermeable second layer with one surface in contact with the other surface of this first layer, and one surface in contact with the other surface of this second layer and the other surface in contact with the other surface of the second layer. a porous third layer having a plurality of grooves perpendicular to the #1 groove; and a porous third layer provided along the groove direction opposite the third layer and the 17th layer and integrated with the second cliff. a gas separation plate formed with a sealed air-impermeable seal part and stacked alternately with the unit power generating element; a storage part in which the electrolyte is stored in the seal part;
Since this reservoir is configured to communicate with the first layer or the third M, electrolyte can be constantly replenished from the reservoir to the first or third layer, so there is no need to frequently replenish electrolytes from the outside, and it can be used for a long period of time. This has the effect of providing a fuel cell that can be operated.
第1図はこの発明の一実施例による燃料電池の基本構成
を示す分解斜視図、第2図は第1図のガス分離板の一部
を示す部分斜視図、第3図はリン酸蒸発量と運転時間の
関係を示す特性図、第4図は従来の燃料電池の基本構成
を示す断面図である。
因において、(1]はマトリックス、(2)および(3
)は電極、(6)はガス分離板、四はガス分離仮止の第
1層、明はガス分離板0の第2層、aηはガス分離板α
Dの第3HJ、@および口はガス分離板αυのシール部
、口は貯溜部である。
なお、図中同一符号は同一、又は相当部分を示す。FIG. 1 is an exploded perspective view showing the basic configuration of a fuel cell according to an embodiment of the present invention, FIG. 2 is a partial perspective view showing a part of the gas separation plate in FIG. 1, and FIG. 3 is an evaporation amount of phosphoric acid. FIG. 4 is a sectional view showing the basic configuration of a conventional fuel cell. In the equation, (1) is a matrix, (2) and (3
) is the electrode, (6) is the gas separation plate, 4 is the first layer of gas separation temporary fixing, light is the second layer of gas separation plate 0, aη is the gas separation plate α
The third HJ, @ and the opening of D are the sealing part of the gas separation plate αυ, and the opening is the storage part. Note that the same reference numerals in the figures indicate the same or equivalent parts.
Claims (4)
の電極とにより構成された単位発電素子、一方の面に複
数の溝を有し多孔質の第1層と、この第1層の他方の面
に一方の面が当接された不透気性の第2層と、この第2
層の他方の面に一方の面が当接され他方の面に上記第1
層の溝と直交する複数の溝を有し多孔質の第3層と、こ
の第3層および上記第1層の両端部に溝方向に添つて設
けられ上記第2層と一体化された不透気性のシール部と
で構成され、上記単位発電素子と交互に積層されるガス
分離板、上記シール部に設けられ上記第1層または第3
層に連通し電解質が貯溜される貯溜部を備えた燃料電池
。(1) A unit power generation element composed of a matrix that holds an electrolyte and a pair of electrodes sandwiching the matrix; a porous first layer with a plurality of grooves on one surface; an air-impermeable second layer having one side abutted against the surface;
One surface is in contact with the other surface of the layer, and the other surface is in contact with the first layer.
a porous third layer having a plurality of grooves orthogonal to the grooves of the layer; and a porous third layer provided along the groove direction at both ends of the third layer and the first layer and integrated with the second layer. an air-permeable sealing section, and a gas separation plate that is stacked alternately with the unit power generation elements;
A fuel cell having a reservoir communicating with a layer and storing an electrolyte.
する特許請求の範囲第1項記載の燃料電池。(2) The fuel cell according to claim 1, wherein the reservoir is a groove whose end is sealed.
とする特許請求の範囲第2項記載の燃料電池。(3) The fuel cell according to claim 2, wherein the groove has a through hole at a sealed end.
する特許請求の範囲第1項ないし第3項のいずれかに記
載の燃料電池。(4) The fuel cell according to any one of claims 1 to 3, wherein a porous body is inserted into the reservoir.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62295508A JPH01137565A (en) | 1987-11-24 | 1987-11-24 | Fuel cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62295508A JPH01137565A (en) | 1987-11-24 | 1987-11-24 | Fuel cell |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH01137565A true JPH01137565A (en) | 1989-05-30 |
Family
ID=17821522
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62295508A Pending JPH01137565A (en) | 1987-11-24 | 1987-11-24 | Fuel cell |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH01137565A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2515994A (en) * | 2013-04-08 | 2015-01-14 | Acal Energy Ltd | Fuel cells |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6220255A (en) * | 1985-07-17 | 1987-01-28 | Toshiba Corp | Fuel cell |
| JPS6298570A (en) * | 1985-10-25 | 1987-05-08 | Kureha Chem Ind Co Ltd | Electrode substrate for end seal-mounting fuel cell and its manufacture |
-
1987
- 1987-11-24 JP JP62295508A patent/JPH01137565A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6220255A (en) * | 1985-07-17 | 1987-01-28 | Toshiba Corp | Fuel cell |
| JPS6298570A (en) * | 1985-10-25 | 1987-05-08 | Kureha Chem Ind Co Ltd | Electrode substrate for end seal-mounting fuel cell and its manufacture |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2515994A (en) * | 2013-04-08 | 2015-01-14 | Acal Energy Ltd | Fuel cells |
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