JPS6188464A - Fuel cell - Google Patents
Fuel cellInfo
- Publication number
- JPS6188464A JPS6188464A JP59208201A JP20820184A JPS6188464A JP S6188464 A JPS6188464 A JP S6188464A JP 59208201 A JP59208201 A JP 59208201A JP 20820184 A JP20820184 A JP 20820184A JP S6188464 A JPS6188464 A JP S6188464A
- Authority
- JP
- Japan
- Prior art keywords
- fuel
- manifold
- pressure
- oxidizer
- electrode
- 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.)
- Granted
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
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04082—Arrangements for control of reactant parameters, e.g. pressure or concentration
- H01M8/04089—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
- H01M8/04104—Regulation of differential pressures
-
- 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
- H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
- H01M8/2465—Details of groupings of fuel cells
- H01M8/2484—Details of groupings of fuel cells characterised by external manifolds
-
- 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
- H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
- H01M8/2465—Details of groupings of fuel cells
- H01M8/2484—Details of groupings of fuel cells characterised by external manifolds
- H01M8/2485—Arrangements for sealing external manifolds; Arrangements for mounting external manifolds around a stack
-
- 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
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
〔発明の利用分野〕
不発明l−1:燃料電池に係シ、特に安全でイg頼性の
高い運転を行なうことがでさる燃料電池に関するもので
ある。DETAILED DESCRIPTION OF THE INVENTION [Field of Application of the Invention] Non-invention 1-1: This invention relates to fuel cells, and particularly relates to fuel cells that can be operated safely and with high reliability.
一般に、燃料の持つ化学エネルギーを電気エネルギーに
直接交換する燃料−池は、燃料の化学エネルギーを熱に
変換し、その熱により得られた熱流体によって機械を作
動させることによシミ気を発生させる従来のエネルギー
変換装置と異なり、熱サイクルの上限であるカルノーサ
イクル以上の効率を発生させることが可能である。この
ため。In general, a fuel pond that directly exchanges the chemical energy of fuel into electrical energy converts the chemical energy of the fuel into heat, and generates stains by operating the machine with the thermal fluid obtained from the heat. Unlike conventional energy conversion devices, it is possible to generate efficiency higher than the Carnot cycle, which is the upper limit of thermal cycles. For this reason.
高効率発電装置として有望視されておシ、研究開発が進
められている。It is seen as a promising high-efficiency power generation device, and research and development is underway.
第1図は、このような燃料電池の代表的な雨成女素を示
す斜視図でるる。FIG. 1 is a perspective view showing a typical example of such a fuel cell.
燃料電池の一般的な単位セルユニットは、セパレータl
、燃料極2、電解質板3、空気極4よシ構成されておシ
、燃料極2には燃料5、空気イタ4には酸素を含む空気
等の酸化剤6が供給される。A general unit cell unit of a fuel cell is a separator l
, a fuel electrode 2, an electrolyte plate 3, and an air electrode 4. The fuel electrode 2 is supplied with fuel 5, and the air plate 4 is supplied with an oxidizing agent 6 such as air containing oxygen.
電解質板3には、′i解質がしみ込ませである。The electrolyte plate 3 is impregnated with 'i solyte.
撚燃料他2および空気極4は多孔質でるシ、鷹科5およ
びば化剤6はそれぞれの電極内を通過して電解質板表面
に到達し、五盾質板より田てくる′冠屏質と反応する。The twisted fuel, etc. 2 and the air electrode 4 are porous, and the falcon 5 and the oxidizing agent 6 pass through each electrode and reach the surface of the electrolyte plate. reacts.
蛋pA質板3はイオンを通過させる力燃料5および酸化
剤6としての空気等を通過させない性質を有している。The protein pA plate 3 has the property of allowing ions to pass therethrough and preventing air and the like acting as the fuel 5 and oxidizing agent 6 from passing therethrough.
セパレータ1は、他のセルとの境界であって、燃料と酸
化剤を分離する役割を持っている。The separator 1 is a boundary with other cells and has the role of separating fuel and oxidizer.
燃料電池は単位セルの出力が微少であるので、単位セル
を複数段積み上げ積層電池を構成させている。Since the output of a unit cell of a fuel cell is very small, a stacked battery is constructed by stacking unit cells in multiple stages.
第2図は積層電池とそれを作動させるに必要な要素を備
えた燃料電池スタックを示す斜視図である。FIG. 2 is a perspective view of a fuel cell stack including stacked cells and the elements necessary to operate them.
第2図において、燃料電池スタックは、セパレータ1、
燃料極2.電解質板3.空気極4よりなる単位セルユニ
ットを積層した積層電池の各側面を、燃料人ロマニュホ
ールド7、燃料用ロマニュホールド8、鹸化剤人ロマニ
ュホ〜ルド9.酸化剤出口マニュホールド10が囲み、
積層な池の上下を端板12ではさみ込んだ後にタイボル
ト11で固定し、かつ圧力容器13が全体を囲むことに
より構成されている。燃料供給管14は、燃料人ロマニ
ュホールド7に接続され、燃料排出管15は燃料量ロマ
ニュホールド8に接続されている。In FIG. 2, the fuel cell stack includes a separator 1,
Fuel electrode 2. Electrolyte plate 3. Each side of a stacked battery in which unit cell units each consisting of an air electrode 4 are stacked is covered with a fuel Roman manifold 7, a fuel Roman manifold 8, a saponifying agent Roman manifold 9. An oxidizer outlet manifold 10 surrounds the
It is constructed by sandwiching the top and bottom of a laminated pond between end plates 12 and then fixing it with tie bolts 11, and surrounding the whole with a pressure vessel 13. The fuel supply pipe 14 is connected to the fuel manifold 7, and the fuel discharge pipe 15 is connected to the fuel quantity manifold 8.
筐た敵化剤供給青16は絃化剤人ロマニュホールド9に
接続され、酸化剤排出管17は酸化削出ロマニュホール
ド10に接続されている。また、圧力容器13の内部に
は不活性ガスが充満されている。The encased oxidizing agent supply pipe 16 is connected to the oxidizing agent manifold 9, and the oxidizing agent discharge pipe 17 is connected to the oxidizing agent manifold 10. Moreover, the inside of the pressure vessel 13 is filled with inert gas.
燃料5は圧力容器13の外部より燃料供給管14によっ
て燃料人ロマニュホールド7内に供給される。燃料人ロ
マニュホールド7に入ったff1Mは積層電池を構成す
る各々のセルの燃料極2に人シ電解質板3を通して空気
極4とイオンの授受を行なった後に燃料用ロマニュホー
ルド8へ排出される。燃料量ロマニュホールド8で回収
された排燃料は燃料排出管15を通して圧力容器内に排
出される。The fuel 5 is supplied from the outside of the pressure vessel 13 into the fuel manifold 7 through a fuel supply pipe 14 . The ff1M that has entered the fuel manifold 7 is discharged to the fuel manifold 8 after passing through the fuel electrode 2 of each cell constituting the stacked battery to exchange ions with the air electrode 4 through the man electrolyte plate 3. Ru. The waste fuel recovered by the fuel quantity Romanifold 8 is discharged into the pressure vessel through the fuel discharge pipe 15.
一方、酸化剤6は圧力容器13の外部よυ酸化剤供給管
16を通し、酸化剤人ロマニュホールド9に供給される
。酸化剤人ロマニュホールド9に入った燃料は、燃料と
同様に各々のセルの空気極4に入す、を解質板3を通し
燃料極2とイオンの授受を行なった後に、酸化削出ロマ
ニュホールド10へ排出される。酸化削出ロマニュホー
ルド10で回収された排酸化剤は酸化剤排出管17によ
って圧力容器13の外に排出される。積層電池は上下に
はさんだ端板12をタイボルト11によシ圧力を加え保
持する。燃料および酸化剤の圧力は、両者の差圧が大き
いと電解質板3より電解質の流出が起きたシ、はなはだ
しい場合には電解質板3を通し燃料5まだは酸化剤6の
クロスオーバを生じたシ、電解質板3の破損を生じる。On the other hand, the oxidizing agent 6 is supplied from the outside of the pressure vessel 13 to the oxidizing agent manifold 9 through an oxidizing agent supply pipe 16. The fuel that has entered the oxidizing manifold 9 is introduced into the air electrode 4 of each cell in the same way as the fuel, and after passing through the electrolyte plate 3 and exchanging ions with the fuel electrode 2, it is oxidized and removed. It is discharged to the Roman Manifold 10. The exhaust oxidant recovered by the oxidation removal manifold 10 is discharged to the outside of the pressure vessel 13 through an oxidant discharge pipe 17. The stacked battery is held by applying pressure to the end plates 12 which are sandwiched between the upper and lower sides by the tie bolts 11. If the pressure difference between the fuel and oxidizer is large, the electrolyte may flow out from the electrolyte plate 3, or in extreme cases, the fuel 5 or oxidizer 6 may cross over through the electrolyte plate 3. , causing damage to the electrolyte plate 3.
このため、両者の差圧は微少に保つ必要がある。また、
圧力容器13内には燃料5および酸化剤6のIJ−り防
止、さらには事故時の安全保持に不活性ガスが燃料5お
よび酸化剤6の圧力よシわずかに高く充満しである。For this reason, it is necessary to keep the differential pressure between the two very small. Also,
The pressure vessel 13 is filled with an inert gas slightly higher than the pressure of the fuel 5 and oxidizer 6 to prevent the fuel 5 and oxidizer 6 from leaking and to maintain safety in the event of an accident.
ところで、燃料電池は、″重力設備であるため。By the way, fuel cells are ``gravity equipment''.
負荷装動の要求に対し応答性よく対応することが必要で
ある。負荷変動は、燃料5およびば化剤6の供給量を変
化させることによう対応する。燃料5および1r化剤6
の供給ジtの変化;は両者の圧力差を大きくしたり、変
動を生じさせ空すい。このため、例えば特開昭57−2
3475号の如きこれらの差圧を常に微少に保持する制
御装置等が提供されている。It is necessary to respond to load application requests with good responsiveness. The load fluctuation corresponds to changing the supply amount of the fuel 5 and the oxidizing agent 6. Fuel 5 and 1R agent 6
Changes in the supply voltage of t may increase the pressure difference between the two or cause fluctuations. For this reason, for example, JP-A-57-2
A control device such as No. 3475 that constantly maintains these differential pressures at a very small level is provided.
しかしながら、これらの装置は、燃料5絃化剤6の圧力
、またはこれらの差圧をセ/すで検出し、検出した信号
によって制御装置が燃料および酸化剤調整用の弁を作動
させるようにしておるために、制御に時間を要し、しか
も急激な圧力変動に追従しがたい欠点がある。また、こ
れらの装置は、圧力容器外に設置することを前提として
いるため、電極間差圧に大きく影響する燃料および酸化
剤人ロマニュホールド内圧を直接制御することが不可能
であった。However, these devices detect the pressure of the fuel 5 and the oxidizing agent 6, or the differential pressure therebetween, and the control device operates the valves for adjusting the fuel and oxidizer based on the detected signal. This has the disadvantage that it takes time to control and is difficult to follow sudden pressure fluctuations. Furthermore, since these devices are assumed to be installed outside the pressure vessel, it has been impossible to directly control the internal pressures of the fuel and oxidizer manifolds, which greatly affect the differential pressure between the electrodes.
本発明の目的は、燃料電池の燃料極側の圧力と空気極側
の圧力との差を常に極少化でさ、負荷変動に対する燃料
および酸化剤の供給量変化に対しても゛、安全かつ信頼
性が高い燃料電池を提供することにある。The purpose of the present invention is to constantly minimize the difference between the pressure on the fuel electrode side and the pressure on the air electrode side of a fuel cell, and to maintain a safe and reliable system even with changes in the supply amount of fuel and oxidizer due to load fluctuations. The objective is to provide a fuel cell with high performance.
本発明は、燃料電池スタックにおいて、圧力容器とマニ
ュホールドの間にはマニュホールド内圧に近い不活性ガ
スが充満している点に注目し、燃料マニュホールドと不
活性ガスとの間および酸化剤マニュホールドと不活性ガ
スとの間の各差圧が一定となるように、マニュホールド
の一部を弾性体で構成して可変容積となし、マニュホー
ルド内外圧力焉をバランスさせるようにしたものである
。The present invention focuses on the fact that in a fuel cell stack, the space between the pressure vessel and the manifold is filled with an inert gas close to the internal pressure of the manifold. In order to keep the differential pressure between the hold and the inert gas constant, a part of the manifold is made of an elastic material to have a variable volume, and the pressure inside and outside the manifold is balanced. .
以下、本発明の実施例を図面に基づいて説明する。 Embodiments of the present invention will be described below based on the drawings.
第3図は1本発明の一実施例を示す平面図である。第3
図において、第2図に示す構成要素と向−のものには同
一の符号を付して説明する。第3図において、積層電池
は燃料極2、空気極4等により構成さnており、その側
面に燃料人ロマニュホールド7、燃料出口マニ二ホール
ド8、酸化剤式ロマニュホールド9.酸化剤出ロマニュ
ホールド10が配置されている。これらの点については
従来例と同様である。また、燃料人ロマニュホールド7
Aには燃料供給管14、燃料用ロマニュホールド8には
燃料排出管15、酸化剤式ロマニュホールド9Aには酸
化剤供給管16、酸化剤出口マニ二ホールド10には酸
化剤排出管17がそれぞれ接続され、積層電池は圧力容
器13が囲まれ圧力容器には不活性ガス供給管19と不
活性ガス排出管20が接続されている。これらの点につ
いても従来例と同様である。本実施例が従来例と異なる
ところは、燃料人ロマニュホールド7Aおよび酸化剤式
ロマニュホールド9Aに弾性体18をそれぞれ取り付け
て可変容積体とした点にある。FIG. 3 is a plan view showing an embodiment of the present invention. Third
In the figure, components opposite to those shown in FIG. 2 are given the same reference numerals and will be explained. In FIG. 3, the stacked battery is composed of a fuel electrode 2, an air electrode 4, etc., and on the side thereof, a fuel manifold 7, a fuel outlet manifold 8, an oxidizer manifold 9. An oxidizing agent output manifold 10 is arranged. These points are similar to the conventional example. In addition, fuel man romanifold 7
A has a fuel supply pipe 14, a fuel romanifold 8 has a fuel discharge pipe 15, an oxidizer type romanifold 9A has an oxidizer supply pipe 16, and an oxidizer outlet manifold 10 has an oxidizer discharge pipe 17. The laminated battery is surrounded by a pressure vessel 13, and an inert gas supply pipe 19 and an inert gas discharge pipe 20 are connected to the pressure vessel. These points are also similar to the conventional example. This embodiment differs from the conventional example in that an elastic body 18 is attached to each of the fuel manifold 7A and the oxidizer manifold 9A to form variable volume bodies.
このような構成になる実施例の作用を説明する。The operation of the embodiment having such a configuration will be explained.
燃料5は、燃料供給管14より燃料人ロマニュホールド
7Aに供給され、燃料極2を通り燃料用ロマニュホール
ド8、燃料排出管15を通シ排出される。酸化剤6は、
酸化剤供給管16より酸化剤式ロマニュホールド9Aに
供給され、空気極4を通り酸化削出ロマニュホールド1
0、酸化剤排出管17を通り排出される。The fuel 5 is supplied to the fuel manifold 7A from the fuel supply pipe 14, passes through the fuel electrode 2, and is discharged through the fuel manifold 8 and the fuel discharge pipe 15. The oxidizing agent 6 is
The oxidizing agent is supplied from the oxidizing agent supply pipe 16 to the oxidizing romanifold 9A, and passes through the air electrode 4 to the oxidizing romanifold 1.
0, is discharged through the oxidizer discharge pipe 17.
ここで、何らかの原因によって燃料まだは酸化剤の供給
圧力が変動した場合、燃料および酸化剤式ロマニュホー
ルド7A、9Aの内圧力変化は。Here, if the supply pressure of the fuel or oxidizer changes for some reason, the internal pressure of the fuel and oxidizer type manifolds 7A and 9A will change.
上記弾性体18を変形させそれぞれに容積変化を生じさ
せる。これにより圧力容器13内の不活性ガス圧力と、
マニュホールド7A、QA内のガス圧力とは自動的にバ
ランスすることになる。The elastic bodies 18 are deformed to cause a change in volume. As a result, the inert gas pressure inside the pressure vessel 13,
The gas pressures in manifolds 7A and QA will be automatically balanced.
本実施例によれば、センサ、制御装置、アクチュエータ
等の機器を必要としないために、高信頼性を保つことが
できる。According to this embodiment, high reliability can be maintained because devices such as sensors, control devices, and actuators are not required.
第4図は本発明の他の実施例を示す平面図である。FIG. 4 is a plan view showing another embodiment of the present invention.
第4図の実施例が第3図に示す実施例と異なるところは
、燃料量ロマニュホールド8Aおよび酸化創出ロマニュ
ホールドIOAの一部に燃料人ロマニュホールド7Aお
よびα化剤人ロマニュホールド9Aと同様に弾性体18
を取り付けて可変容積体が構成された点にある。ここで
、それぞれの弾性体18は圧力容器内圧とそれぞれのマ
ニュホールド7A、8A、9A、IOAの内圧とがバラ
ンスするように、予め調整されている。The difference between the embodiment shown in FIG. 4 and the embodiment shown in FIG. 3 is that a part of the fuel quantity Romanifold 8A and the oxidation creation Romanifold IOA includes a fuel manifold 7A and a pregelatinizing agent manifold. Elastic body 18 similar to 9A
The point is that a variable volume body is constructed by attaching the . Here, each elastic body 18 is adjusted in advance so that the internal pressure of the pressure vessel and the internal pressure of each manifold 7A, 8A, 9A, and IOA are balanced.
この実施例では、燃料極および空気極入口圧力の制御に
加え、燃料極および空気極出口の圧力も制御することが
可能であるため、燃料極と空気極の差圧をより小さくで
きる。In this embodiment, in addition to controlling the fuel electrode and air electrode inlet pressures, it is also possible to control the fuel electrode and air electrode outlet pressures, so that the differential pressure between the fuel electrode and the air electrode can be further reduced.
第5図は本発明のさらに他の実施例を示す平面図である
。第5図に示す実施例が第3図に示す実施例と異なると
ころは、マニュホールド7B。FIG. 5 is a plan view showing still another embodiment of the present invention. The embodiment shown in FIG. 5 differs from the embodiment shown in FIG. 3 in the manifold 7B.
9Bの弾性体18の弾性力を小さなものとし、補助の弾
性体22をマニュホールドに取υ付けだ点にある。The elastic force of the elastic body 18 of 9B is made small, and the auxiliary elastic body 22 is attached to the manifold.
この実施例では、マニュホールド内圧と圧力容器13の
内圧とを予めバランスさせる弾性体22をマニュホール
ドとは別にすることができるので、初期設定を容易にで
きる。In this embodiment, since the elastic body 22 that balances the internal pressure of the manifold and the internal pressure of the pressure vessel 13 in advance can be provided separately from the manifold, initial settings can be made easily.
同、マニュホールドに弾性体を設置するとともにダンパ
ーを併用することにより、より安定に動作させることも
できる。By installing an elastic body on the manifold and using a damper, it is possible to operate more stably.
この実施例では、マニュホールドの過度の動きを防止し
、安定な差圧制御を行なえる。In this embodiment, excessive movement of the manifold can be prevented and stable differential pressure control can be performed.
以上述べたように本発明によれば、響料極側の圧力と空
気極側の圧力差を可変容積としたマニュホールドで常に
極少化することができるので、圧力の急変等が生じても
安全かつ信頼性の高い運転を行なえる効果がある。As described above, according to the present invention, the pressure difference between the pressure on the sound electrode side and the air electrode side can always be minimized using a manifold with variable volume, so it is safe even if sudden changes in pressure occur. This also has the effect of allowing highly reliable operation.
第1図は燃料電池の基本構成要素を示す斜視図、第2図
は燃料電池のスタック構成を示す斜視図、第3図は本発
明の一実施例を示す平面図、第4図は同地の実施例を示
す平面図、第5図は同地の実施例を示す平面図である。
2・・・燃料極、3・・・電解質板、4・・・空気極、
7,8・・・燃料マニュホールド、9.10・・・1.
ff 化剤マニュホールド、13・・・圧力容器、18
・・・弾性体。FIG. 1 is a perspective view showing the basic components of a fuel cell, FIG. 2 is a perspective view showing a stack configuration of the fuel cell, FIG. 3 is a plan view showing an embodiment of the present invention, and FIG. FIG. 5 is a plan view showing an example of the same location. 2... Fuel electrode, 3... Electrolyte plate, 4... Air electrode,
7, 8...Fuel manifold, 9.10...1.
ff Curing agent manifold, 13...pressure vessel, 18
...Elastic body.
Claims (1)
化極を設け、これらをセパレータで挾着してなるセルユ
ニットを積層して積層電池を構成し、該積層電池の各側
面にマニュホールドを配設し、当該マニュホールドに燃
料供給管、排出管と酸化剤供給管、排出管とをそれぞれ
接続し、前記積層電池を不活性ガスを充満させた圧力容
器内に収容してなる燃料電池において、少なくとも燃料
および酸化剤の供給側マニュホールドが弾性体を一部に
用いて形成した可変容積体であることを特徴とする燃料
電池。1. A fuel electrode is provided on one surface of an electrolyte plate and an oxidation electrode is provided on the other surface, and cell units formed by sandwiching these with separators are stacked to form a stacked battery, and each side of the stacked battery is A manifold is disposed in the manifold, a fuel supply pipe, a discharge pipe, an oxidizer supply pipe, and a discharge pipe are respectively connected to the manifold, and the stacked battery is housed in a pressure vessel filled with an inert gas. 1. A fuel cell characterized in that at least a fuel and oxidant supply side manifold is a variable volume body formed using an elastic body in part.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59208201A JPS6188464A (en) | 1984-10-05 | 1984-10-05 | Fuel cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59208201A JPS6188464A (en) | 1984-10-05 | 1984-10-05 | Fuel cell |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6188464A true JPS6188464A (en) | 1986-05-06 |
| JPH0322026B2 JPH0322026B2 (en) | 1991-03-26 |
Family
ID=16552334
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59208201A Granted JPS6188464A (en) | 1984-10-05 | 1984-10-05 | Fuel cell |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6188464A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6481176A (en) * | 1987-09-24 | 1989-03-27 | Hitachi Ltd | Fuel cell |
| WO2010016247A1 (en) * | 2008-08-07 | 2010-02-11 | パナソニック株式会社 | Fuel cell stack and fuel cell system employing the same |
| US20210344032A1 (en) * | 2018-06-07 | 2021-11-04 | Audi Ag | Fuel cell device |
| US20210408571A1 (en) * | 2018-11-12 | 2021-12-30 | Audi Ag | Fuel cell device |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8028344B2 (en) | 2005-06-17 | 2011-10-04 | Artisent, Inc. | Hinged attachment of headgear to a helmet |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58165276A (en) * | 1982-03-26 | 1983-09-30 | Fuji Electric Co Ltd | Manifold structure of fuel cell |
-
1984
- 1984-10-05 JP JP59208201A patent/JPS6188464A/en active Granted
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58165276A (en) * | 1982-03-26 | 1983-09-30 | Fuji Electric Co Ltd | Manifold structure of fuel cell |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6481176A (en) * | 1987-09-24 | 1989-03-27 | Hitachi Ltd | Fuel cell |
| WO2010016247A1 (en) * | 2008-08-07 | 2010-02-11 | パナソニック株式会社 | Fuel cell stack and fuel cell system employing the same |
| JP5077358B2 (en) * | 2008-08-07 | 2012-11-21 | パナソニック株式会社 | Fuel cell stack and fuel cell system using the same |
| US20210344032A1 (en) * | 2018-06-07 | 2021-11-04 | Audi Ag | Fuel cell device |
| US11735759B2 (en) * | 2018-06-07 | 2023-08-22 | Audi Ag | Fuel cell device |
| US20210408571A1 (en) * | 2018-11-12 | 2021-12-30 | Audi Ag | Fuel cell device |
| US11721827B2 (en) * | 2018-11-12 | 2023-08-08 | Audi Ag | Fuel cell device |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0322026B2 (en) | 1991-03-26 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP3605126B2 (en) | Components for incorporation into process control equipment | |
| JPH1131520A (en) | Polymer electrolyte fuel cell | |
| US20080138692A1 (en) | Fuel cell apparatus | |
| JP2701522B2 (en) | Fuel cell generator | |
| CN101271984A (en) | fuel cell stack | |
| CN101425590A (en) | Hydrogen gas security protection system for fuel cell engine | |
| JPS6188464A (en) | Fuel cell | |
| JP4062798B2 (en) | Fuel cell and fuel cell assembly | |
| JPS63211573A (en) | Solid electrolyte fuel battery | |
| JPS63119166A (en) | Fuel battery | |
| JP3258378B2 (en) | Fuel cell | |
| JPH08306381A (en) | Stacked fuel cell | |
| JPH0521083A (en) | Fuel cell | |
| JP2007066625A (en) | Fuel cell stack | |
| JPH01298653A (en) | Fuel cell | |
| JPH05242903A (en) | Fuel cell stack | |
| KR102664114B1 (en) | Air shut off valve apparatus for fuel cell system | |
| JPS62246266A (en) | Fuel cell device | |
| CN100517844C (en) | Normal pressure air suction type operation and cooling fuel cell | |
| JPS6246951B2 (en) | ||
| JP3958423B2 (en) | Power generator | |
| JP2583417Y2 (en) | Fuel cell generator | |
| JPH04294066A (en) | Fuel cell | |
| JPH07176316A (en) | Heat exchanger for flat plate solid oxide fuel cell | |
| JPH06111840A (en) | Fuel cell |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |