JPS58157062A - Layer-built fuel cell - Google Patents

Layer-built fuel cell

Info

Publication number
JPS58157062A
JPS58157062A JP57039911A JP3991182A JPS58157062A JP S58157062 A JPS58157062 A JP S58157062A JP 57039911 A JP57039911 A JP 57039911A JP 3991182 A JP3991182 A JP 3991182A JP S58157062 A JPS58157062 A JP S58157062A
Authority
JP
Japan
Prior art keywords
fuel
oxidizer
flow paths
flow path
gas separation
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
Application number
JP57039911A
Other languages
Japanese (ja)
Inventor
Yoichi Mizumoto
水本 洋一
Mitsuie Matsumura
光家 松村
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Electric Corp
Original Assignee
Mitsubishi Electric Corp
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 Mitsubishi Electric Corp filed Critical Mitsubishi Electric Corp
Priority to JP57039911A priority Critical patent/JPS58157062A/en
Publication of JPS58157062A publication Critical patent/JPS58157062A/en
Pending legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/02Details
    • H01M8/0202Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/0247Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the form
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/24Grouping of fuel cells, e.g. stacking of fuel cells
    • H01M8/2457Grouping of fuel cells, e.g. stacking of fuel cells with both reactants being gaseous or vaporised
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/02Details
    • H01M8/0202Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/0258Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/02Details
    • H01M8/0271Sealing or supporting means around electrodes, matrices or membranes
    • H01M8/0273Sealing or supporting means around electrodes, matrices or membranes with sealing or supporting means in the form of a frame
    • 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

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

PURPOSE:To equalize the flow rates of a fuel and an oxidizer supplied from manifolds by providing the inflow parts of the fuel and the oxidizer flow paths of a gas-separating plate with throats having a sectional area smaller than the sectional area of the flow paths. CONSTITUTION:A unit cell consisting of a fuel electrode, an electrolyte mixture and an oxidizer electrode, is attached between gas-separating plates 6 each of which is provided with fuel flow paths 6a and oxidizer flow paths 6b on its upper and lower surfaces in such a manner that the fuel flow paths 6a are perpendicular to the oxidizer flow paths 6b. A fuel and an oxidizer, respectively, are fed from manifolds 5a and 5b are discharged into other manifolds 5a and 5b. In addition, cylindrical throats 7a and 7b are provided at the inflow parts of the fuel flow paths 6a and the oxidizer flow paths 6b of each gas-separating plate 6. As a result, since a pressure loss caused due to the throat 7a or 7b becomes equal to or higher than a pressure loss caused due to the flow path 6a or 6b, the flow rates of the fuel and the oxidizer supplied from the manifolds 5a and 5b can be almost equalized.

Description

【発明の詳細な説明】 この発明は、Ili層形組料亀池、特にその燃料流路又
は酸化剤fh路の構造に関するものでみる。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an Ili layered composite, particularly to the structure of its fuel flow path or oxidant fh path.

亀1−は従来の&胸形組料亀池の要部構成を示す分解針
視りで、(1)は上・下面それぞれに互いに直交する方
向の矩形状の燃料&ji& (Ia)と酸化剤流路(1
b)を有するガス分離板、(2)は乙のガス分離板(υ
の−に装着されて動作する燃料電極、電解質マトリック
ス、酸化剤電極から構成される単電池、(3) laこ
の単電池(2)の周囲に窓枠状に装着されたガスケット
である。
Kame 1- is a disassembly needle view showing the main part configuration of the conventional & chest-shaped composite Kameike, (1) shows rectangular fuel &ji& (Ia) and oxidant flow in directions orthogonal to each other on the upper and lower surfaces respectively. Road (1
(2) is the gas separation plate (υ
(3) A gasket is attached around this unit cell (2) in the shape of a window frame.

次に動作について説明する。ガス分離板(1)と単電池
(2」とを交互に、燃料流路(1a)と酸化剤流路(l
b)の方向をそれぞれ総て一致させて、駁当するガス分
離板(1)の流路向と単電池(2)の電極向とを&看さ
せて、複数輌槓層して槓脂形燃料翫池(4)とする。こ
のとき、ガスケット(3)をガス分離板(1)と単電池
(2)との間に挿入して、燃料および酸化剤が紙当外の
汎略に漏れることを防止する。仁のようにして組立てた
積層形燃料亀池(4)を創作させる場合の構成を、勤2
−の断向平面函にて説明する。
Next, the operation will be explained. The gas separation plate (1) and the unit cell (2) are alternately connected to the fuel flow path (1a) and the oxidant flow path
By aligning the directions of (b) and the direction of the flow path of the corresponding gas separation plate (1) and the direction of the electrode of the unit cell (2), multiple units are layered to form a resin-type fuel. Let's call it Kanike (4). At this time, a gasket (3) is inserted between the gas separation plate (1) and the unit cell (2) to prevent the fuel and oxidizer from leaking to other areas than the paper. The configuration for creating a stacked fuel Kameike (4) assembled in the same way as Jin
This will be explained using a cross-section plane box.

撫層形燃料亀池(4)の周囲に、燃料流路と酸化剤流路
のそれぞれに燃料と酸化剤を供給するために、骸当する
汎略の総てを振う箱体形状の燃料および酸化剤供給用の
流路となる燃料マニホールド(6a)および酸化剤マニ
ホールド(5b)を装着する。
Around the layered fuel Kameike (4), in order to supply fuel and oxidizer to each of the fuel flow path and oxidizer flow path, there is a box-shaped fuel and A fuel manifold (6a) and an oxidizer manifold (5b), which serve as flow paths for supplying an oxidizer, are installed.

燃料マニホールド(5a)および酸化剤マニホールド(
5b)に燃料おまひ酸化剤かそれぞれ供給されると、多
数本か並夕0的に起振された槁造である燃料&路(1a
)および酸化剤流路(lb)に、燃料および酸化剤かそ
れぞれ流れる。燃料流I@(la)および酸化剤旅路(
tb)に流入したm科および酸化剤は、該当する燃料%
LIIIIおよび販イし剤電極の中を拡叡した後、単電
池(2)において電気化学的反応に寄与してtafht
jIL力の発生と反応による水分生成を起こす。このと
き発生した直拠亀力は、単電池(2)か極層方向にガス
分離板(1)を介してぬ列接続されており、槓層形燃料
亀池(4)の板上取と奴下級のカス分離板より外部の一
気1鮎へ導ひかれる。なお、反応に奇与しなかつtコ米
反応の燃料および欧化剤は、該当する燃料frL細(1
a)と酸化剤流路(1b)を経由して、該当する出口側
の燃料マニホールド(6a)と酸化剤マニホールド(6
b)から外部へ入出する。ここで、&胸数が増加するに
つれて、燃料と酸化剤の′kf11分布を均一にして槓
膚形燃料先池の性能を向上させるtこめに、該当するマ
ニホールドの物造もしくは該当する派略の形状を工夫す
るごとかますます必要となってきtこ。
Fuel manifold (5a) and oxidizer manifold (
When 5b) is supplied with fuel and oxidizer, the fuel & road (1a
) and the oxidizer flow path (lb), respectively. Fuel flow I@(la) and oxidizer journey (
tb) and the oxidizer entered into the corresponding fuel%
After examining the inside of LIII and the electrode, tafht contributes to the electrochemical reaction in the cell (2).
jIL force is generated and water is produced by reaction. The direct-base torque generated at this time is due to the fact that the single cells (2) are connected in series in the pole direction without intervening the gas separation plate (1). It is led to the external ayu from the lower grade waste separation plate. In addition, the fuel and Europeanization agent for the reaction that do not contribute to the reaction are the corresponding fuel frL (1
a) and the oxidizer flow path (1b), the corresponding outlet side fuel manifold (6a) and oxidizer manifold (6)
b) External entry/exit. Here, as the number of breasts increases, the corresponding manifold structure or the corresponding derivative should be used to uniformize the 'kf11 distribution of fuel and oxidant and improve the performance of the scalloped fuel reservoir. The more I devised the shape, the more I needed it.

従来の燃料旅紬又(、!酸化剤流路は以上のような単純
な矩形状のみの涌造になっているので、k料又は酸化剤
の&路の流星分布を均一にするの1よ困難であり、した
かつて反応に寄与する以上の過剰な燃料又は酸化剤を供
給すること力ふ必要である欠点かめった。
The conventional fuel travel path (,! Since the oxidizer flow path has only a simple rectangular shape as shown above, it is difficult to make the meteor distribution of the K material or oxidizer & path uniform. This method is difficult and suffers from the disadvantage that it is necessary to supply excess fuel or oxidant beyond that contributing to the reaction.

この発明は上記のような従来のもQ)の欠点を除去す4
tこめになされたもので、燃料流路又Gま酸化剤fj+
b紬盛こに路動面積が他の施路断面積より小さも)喉部
を設けることにより、燃料又は酸イヒ剤Q〕流婁分布を
垢−にしようとするものである。
This invention eliminates the above-mentioned drawbacks of the conventional method (Q).
This was done at the time of the fuel flow path or the oxidizer fj+
(b) By providing a throat section (the cross-sectional area of which is smaller than the other sections), the flow distribution of fuel or acid chloride (Q) is intended to be reduced.

以下、この発明の一実施例を1について説明りる。11
J8図において、(6)は燃料および酸化剤の流入側の
一部分を拡大して示したガス分離板、(6a)はこのガ
ス分離板(6)の−面に複数本の平行に設けた矩形状の
燃料流路、(6b)は上記ガス分離板(6)の上ic燃
料旅路(6a)の対向する面に、上記燃料流路(6a)
と直交する方向に複数本の平行に設はすこ矩形状の嘔化
剤&紬、(7a)は上記燃料流路(6a)の流入部分に
設けた円筒状の燃料vfk都、(7b)は上dじ酸化剤
流路(6b)の流入部分に設けた円筒状の酸化剤喉部で
ある。
Hereinafter, one embodiment of the present invention will be described. 11
In Figure J8, (6) is an enlarged view of a portion of the inflow side of the fuel and oxidizer, and (6a) is a plurality of rectangles provided in parallel on the negative side of the gas separation plate (6). The fuel flow path (6b) in the shape of
(7a) is a cylindrical fuel vfk provided in the inflow part of the fuel flow path (6a), (7b) is This is a cylindrical oxidant throat provided at the inflow portion of the oxidant flow path (6b) as shown above.

次に動作について&明する。このガス分離板(6)を用
いて樵ノー形燃料亀池を構成して動作させる方法は、従
来のガス分離板(1)による一層形燃料−池(4)を禍
成して動作させる場合とほぼ向−である。
Next, I will explain the operation. The method of configuring and operating a woodcutter no-type fuel pond using this gas separation plate (6) is the same as the method of constructing and operating a single-layer fuel pond (4) using the conventional gas separation plate (1). It is almost in the direction.

すなわち、ガス分離板(60こよる桓鳩形燃料亀池の場
合も、第2因におい“C説明したように画成する。
That is, in the case of the gas separation plate (60 pieces), it is defined as explained in "C" in the second factor.

ここで、燃料マニホールド(5a)および酸化剤マニホ
ールド(5b)に燃料および酸化剤かそれぞれ供給され
ると、、それぞれの流入部分に設(ブた燃料喉sc’r
a)および酸化剤喉5(Wb)を通過して、多数本が並
列的に起振された燃料流路(6a)および酸化剤M路(
6b)に燃料および酸1ヒ創か扼れて、単電池(2)に
おいて亀気化学市反応か生じる。次に、燃料喉部(7a
)と酸化剤1lIk部(7b)つまり喉部に胸して、そ
の動作につい°C詳細に説明する。峡部の派略#1SI
fLl執は他の流路部分の断曲伽より小さく(例えば1
710札度)し、喉部の灸さは窓枠形状のガスケット(
3)の窓枠幅とほぼ等しくする。これにより、旅人して
くる燃料もしくは酸化剤の配鴨による圧損は、喉部に寄
因するものかfIrL路すし分をこ寄因するものより同
等以上の飯になる。しtこかつて、マニホールドから供
給される燃料もしくは酸化剤の入路それぞれの九九分布
1ハ喉都による圧損増加によって、はぼ均一になる。ま
た、窓枠形状のガスケット(3)は、ガス分離板(6)
と単−池(2)とにより、ガス分離板の8縁が平らなた
め全体に均一に圧着されることになり気密性が向上する
Here, when the fuel and oxidizer are supplied to the fuel manifold (5a) and the oxidizer manifold (5b), a fuel throat sc'r is installed at each inflow portion.
a) and the oxidizer throat 5 (Wb), and the fuel flow path (6a) and the oxidizer M path (
6b) When the fuel and acid are mixed, a chemical reaction occurs in the cell (2). Next, the fuel throat (7a
) and the oxidizer 1lIk part (7b), that is, the throat part, and its operation will be explained in detail. Isthmus Sect #1SI
fLl bending is smaller than the bending of other flow path parts (for example, 1
710 degrees), and the moxibustion of the throat is treated with a window frame-shaped gasket (
Make it approximately equal to the window frame width in 3). As a result, the pressure loss due to the distribution of fuel or oxidizer coming from the traveler will be equal to or greater than the pressure loss caused by the throat or fIrL route. Until then, the distribution of fuel or oxidizer supplied from the manifold becomes almost uniform due to the increase in pressure drop due to the inlet. In addition, the window frame-shaped gasket (3) is connected to the gas separation plate (6).
Since the eight edges of the gas separation plate are flat, the eight edges of the gas separation plate are uniformly crimped over the entire plate, resulting in improved airtightness.

又、峡りトの形状については、第8図に示しt二円筒形
状でなく、第4図に示す矩形状のものなども長石できる
。この場合、ガス分離板(6Jのプレスエ札などの製作
の′6易性は第4因の矩形状のものか優れており、ガス
ケット(3)の気密性では第8図の円部形状のものか有
利である。
Furthermore, regarding the shape of the gorge, instead of the cylindrical shape shown in FIG. 8, feldspars can also have a rectangular shape as shown in FIG. 4. In this case, the ease of manufacturing gas separation plates (such as 6J press notes) is superior to that of the rectangular shape shown in factor 4, and the airtightness of the gasket (3) is superior to that of the circular shape shown in Figure 8. It is advantageous.

なお、上記実施机では喉5(7a)と(7b)を旅路(
6a)と(6b)の流入部分に設けたものを示したか、
&k(7a)と(7b)を流* (6a)と(6b)の
派出部分、中r#!!lJ部分、もしくは流入部分と振
出部分の絢鉤に設けてもよい。
In addition, in the above implementation machine, the throats 5 (7a) and (7b) are connected to the journey (
Did you show what is installed at the inflow part of 6a) and (6b)?
&k (7a) and (7b) flow * Outgoing parts of (6a) and (6b), medium r#! ! It may be provided on the hook of the lJ part or the inflow part and the swinging part.

しかし、臨入部分に喉部を設けると、扼入方ス(燃料又
は酸化剤)の全りに対して圧損を影会させ得るが、振出
部分に設けると汎大ガスhから清貧されたガス篇を蓋引
いtこ残りの瓢にしか圧損か形動しないので、前者の方
かJ+:損か多く、旅−分布か均一になりやすい。
However, if a throat is provided in the inlet part, the pressure drop will be affected for all of the inlet gas (fuel or oxidizer), but if it is provided in the outlet part, the gas purified from the general gas h will be affected. Since the pressure loss only changes when the lid is pulled and the remaining gourd, the former tends to be more J+, and the distribution tends to be more uniform.

また、上記実り帆ではガス分賑板の旅路について説明し
たか、リブ付1kmと呼はれている電機にに絡かある場
合でも九細中に汎略動−一か他のか。
In addition, in the above-mentioned fruitful sail, did we explain the journey of the gas board, or even if it is caught in the electric machine called 1 km with ribs, is it general movement in nine narrow areas - one or other?

略断向横より小さい眼部を設けれは、上記実り沙りと同
様の効果を拠する。
Providing an eye portion that is smaller than the width of the cross section has the same effect as the above-mentioned effect.

以上のように、この発明によれは、燃料又は眼化剤の訛
略中に施IkI断面情か他の旅路断面積より小さい喉部
を設けたので、tkLkに旅人する扼入カスの@r、n
分布を均一にすることができる。
As described above, according to the present invention, since a throat portion is provided in the middle of the fuel or ophthalmic agent, the cross-sectional area of the cross-sectional area of the fuel or the ophthalmic agent is smaller than the cross-sectional area of other travel routes. ,n
Distribution can be made uniform.

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

ル1−は従来の慎ノー形f&料亀池の被部檎成をかす分
解斜視1、第2I81は他層形に、料翫池の栖成と1作
を示す1曲乎面−1第8−はこの晃明の一人鳳伝による
ガス分&板の喉部と旅路を示す拡大部分斜視因、船4図
はこの発明の峡部の他の杉状帆を小すガス分離板の拡大
部分斜視1である。 h中、(1)はガス分離板、(2)は単電池、(3)は
ガスケット、(6)はガス分離板、(6a)は焼料流路
、(6b)は除イし剤流路、(7a)はmy#Jtii
x&、(7b)は除化剤喉部である。 なお、1中、同一符号は同一、又は相当部分をボす。 代理人  為 封 値 − 第1図 IN2図 ゛第3図 A b 第4図 手続補正書(自発) 昭和 571盾 鴨 1、事件の表示    特願昭6丁−89111号2、
発明の名称 積層形蝙科電池 3、補正をする者 6、 補正の対象 明細書の特許請求の範囲−P4/A 6、補正の内容 明細書の特許請求の範囲44=を別紙のとおり訂正する
。 フ、 添付書類の目録 補正後の特許請求の範囲を記載した書面 1通以上 特許請求の範囲 (υ燃料1轟−電解質マトリックス、酸化剤電極及びガ
ス分離板が順次複数個積層され、上記ガス分離板と燃料
電極間暑ζ燃料流路が形成されると共に、上記酸化剤電
極とガス分離板間暑と酸化剤流路が形成された積層形燃
料電池において、上記流路中に流路断面積が他の流路断
面積より小さい喉部を設けたことを特徴とする積層形燃
料電池。 (2)喉部を流路の流入部分に設けたことを特徴とする
特許請求の範囲第1項記載の積層形燃料電池。。
Le 1- is an exploded perspective view 1 that shows the conventional Shinno-type f &Ryogameike's cover part 1, and 2I81 is a multi-layered type, and 1 curved surface-1 shows the 1st work of Ryokageike. - is a perspective view of an enlarged part showing the throat and travel path of the gas portion and plate according to Komei's Hitori Hoden, Figure 4 is a perspective view of an enlarged part of the gas separation plate that reduces the other cedar-shaped sail of the isthmus of this invention. It is. In h, (1) is a gas separation plate, (2) is a cell, (3) is a gasket, (6) is a gas separation plate, (6a) is a charring material flow path, and (6b) is a removal agent flow. road, (7a) is my#Jtii
x&, (7b) is the demulcent throat. Note that the same reference numerals in 1 indicate the same or corresponding parts. Seal price for agent - Figure 1 IN2 Figure 3 A b Figure 4 Procedural amendment (voluntary) Showa 571 shield Kamo 1, case indication Patent application Showa 6-89111 No. 2,
Title of the invention: Multilayer Fate Battery 3. Person making the amendment: 6. Claims of the specification to be amended - P4/A 6. Contents of the amendment: Claims 44 of the specification are corrected as shown in the attached sheet. . F. A document stating the scope of claims after the amendment to the list of attached documents; one or more copies of the scope of claims (υFuel 1 - A plurality of electrolyte matrix, oxidizer electrodes and gas separation plates are laminated in sequence, and the above gas separation In a stacked fuel cell in which a fuel flow path is formed between the plate and the fuel electrode, and an oxidant flow path is formed between the oxidizer electrode and the gas separation plate, the flow path has a cross-sectional area in the flow path. A stacked fuel cell characterized in that a throat section is provided with a cross-sectional area smaller than that of the other flow channels.(2) Claim 1, characterized in that the throat section is provided at an inlet portion of the flow channel. The stacked fuel cell described.

Claims (2)

【特許請求の範囲】[Claims] (1)燃料電池、電解質マトリックス、酸化剤電極及び
ガス分離板が順次複数個積層され、上記ガス分離板と燃
料電極−に燃料流路か形成されると共に、上記酸化剤1
1!c極とガス分離板間に酸化剤に紬か形成された槓膚
形燃料亀池において、上記fIrL略中に流路断iio
&か他の旅路断面積より小さい喉部を設けたことを特徴
とする槓層形&y#+亀池。
(1) A plurality of fuel cells, an electrolyte matrix, an oxidant electrode, and a gas separation plate are sequentially stacked, a fuel flow path is formed between the gas separation plate and the fuel electrode, and the oxidant 1
1! In the shell-shaped fuel Kameike where the oxidizer is formed between the c electrode and the gas separation plate, the flow path is interrupted in the above fIrL.
&Y#+Kameike is characterized by having a throat section smaller than other cross-sectional areas.
(2)喉部を流路の汎入部分に設けたことを特徴とする
特許請求の範囲第1項記戦の横脂形燃料−池。
(2) The horizontal oil type fuel pond according to claim 1, characterized in that the throat is provided at the inlet portion of the flow path.
JP57039911A 1982-03-12 1982-03-12 Layer-built fuel cell Pending JPS58157062A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57039911A JPS58157062A (en) 1982-03-12 1982-03-12 Layer-built fuel cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57039911A JPS58157062A (en) 1982-03-12 1982-03-12 Layer-built fuel cell

Publications (1)

Publication Number Publication Date
JPS58157062A true JPS58157062A (en) 1983-09-19

Family

ID=12566124

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57039911A Pending JPS58157062A (en) 1982-03-12 1982-03-12 Layer-built fuel cell

Country Status (1)

Country Link
JP (1) JPS58157062A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6212269U (en) * 1985-07-05 1987-01-24
JPS6262765U (en) * 1985-06-10 1987-04-18
JPS63181265A (en) * 1987-01-23 1988-07-26 Toshiba Corp Fuel cell
JPS63291364A (en) * 1987-05-25 1988-11-29 Toshiba Corp Control of fuel cell voltage distribution
JPH01246768A (en) * 1988-03-29 1989-10-02 Toshiba Corp Electrode of fuel cell
JP2008276977A (en) * 2007-04-25 2008-11-13 Nippon Telegr & Teleph Corp <Ntt> Solid oxide fuel cell

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6262765U (en) * 1985-06-10 1987-04-18
JPS6212269U (en) * 1985-07-05 1987-01-24
JPS63181265A (en) * 1987-01-23 1988-07-26 Toshiba Corp Fuel cell
JPS63291364A (en) * 1987-05-25 1988-11-29 Toshiba Corp Control of fuel cell voltage distribution
JPH01246768A (en) * 1988-03-29 1989-10-02 Toshiba Corp Electrode of fuel cell
JP2008276977A (en) * 2007-04-25 2008-11-13 Nippon Telegr & Teleph Corp <Ntt> Solid oxide fuel cell

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