JPH0754711B2 - Fuel cell device - Google Patents
Fuel cell deviceInfo
- Publication number
- JPH0754711B2 JPH0754711B2 JP58240997A JP24099783A JPH0754711B2 JP H0754711 B2 JPH0754711 B2 JP H0754711B2 JP 58240997 A JP58240997 A JP 58240997A JP 24099783 A JP24099783 A JP 24099783A JP H0754711 B2 JPH0754711 B2 JP H0754711B2
- Authority
- JP
- Japan
- Prior art keywords
- pressure
- manifold
- gas
- fuel cell
- reaction gas
- 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.)
- Expired - Lifetime
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
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/30—Arrangements for facilitating escape of gases
- H01M50/317—Re-sealable arrangements
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/30—Arrangements for facilitating escape of gases
- H01M50/317—Re-sealable arrangements
- H01M50/325—Re-sealable arrangements comprising deformable valve members, e.g. elastic or flexible valve members
- H01M50/333—Spring-loaded vent valves
-
- 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
- Y02E60/10—Energy storage using batteries
-
- 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)
- Fuel Cell (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
Description
【発明の詳細な説明】 〔発明の属する技術分野〕 本発明は燃料ガスのもつ化学エネルギーを電気化学反応
により電気エネルギーに変換する燃料電池装置に関す
る。Description: TECHNICAL FIELD The present invention relates to a fuel cell device for converting chemical energy of fuel gas into electric energy by an electrochemical reaction.
燃料と酸化剤とを電気化学的に反応させることにより燃
料のもつ化学エネルギーを直接電気エネルギーに変換し
て電力をとり出す装置として燃料電池がある。There is a fuel cell as a device that directly converts the chemical energy of the fuel into electric energy by extracting the electric power by reacting the fuel and the oxidant electrochemically.
その具体的構成を第一世代型の燐酸電解質燃料電池を例
にとり説明すると以下のようである。第1図(a)は発
電ユニットの模式図を示したものである。触媒層1を塗
着した一対の対向するガス拡散電極(アノード2,カソー
ド3)間に電解質を保持したマトリックス4を介在させ
一体化して形成した単電池の両側にガス流路の溝を設け
た導電性のセパレータ5を置き、燃料ガス6及び酸化剤
ガス7を第1図(b)に示す通り通常直交方向に流し起
電反応を行わせる。なお第1図(b)は第1図(a)の
平面図である。この単位電池の出力はたかだか1V弱であ
るので、これらの単位電池を多数個積層して発電に供す
る。第2図(a),(b)に示したような締付けバー8
及び締付けロッド9にて締結し、又この周縁部にガス供
給及び排出用のマニホールド10a,10b,10c,10dをとりつ
けて積層電池(スタック)を構成する。The specific structure of the first-generation phosphoric acid electrolyte fuel cell will be described below as an example. FIG. 1 (a) shows a schematic view of the power generation unit. Grooves of gas flow paths were provided on both sides of a unitary cell formed by integrating a matrix 4 holding an electrolyte between a pair of opposed gas diffusion electrodes (anode 2 and cathode 3) coated with a catalyst layer 1. A conductive separator 5 is placed, and a fuel gas 6 and an oxidant gas 7 are normally flowed in a direction orthogonal to each other as shown in FIG. Note that FIG. 1 (b) is a plan view of FIG. 1 (a). Since the output of this unit battery is at most 1V, a large number of these unit batteries are stacked for power generation. Tightening bar 8 as shown in FIGS. 2 (a) and 2 (b)
And a fastening rod 9, and manifolds 10a, 10b, 10c, and 10d for gas supply and discharge are attached to the peripheral portion to form a stacked battery (stack).
また電池出力は供給ガスの圧力上昇により反応種の濃度
(活量)を増大して起電反応が促進されるのでマニホー
ルド内の圧力を高めた方が良いが、マニホールドと積層
体側面外周部との気密部の耐圧性が大きくないためスタ
ックは圧力容器12内に収納し、大気圧との圧力差は圧力
容器のフランジ部で受けるようにしている。As for the battery output, the pressure in the supply gas increases the concentration (activity) of the reactive species and promotes the electromotive reaction, so it is better to increase the pressure in the manifold. Since the pressure tightness of the airtight portion is not so large, the stack is housed in the pressure vessel 12, and the pressure difference from the atmospheric pressure is received by the flange portion of the pressure vessel.
また燃料ガスと酸化剤ガスがマトリックス層を通して交
差混合(クロスオーバー)しないように、燃料としての
天然ガス改質ガス(H2 80%+CO2 20%)と酸化剤としての空
気の供給圧力を例えば容器内の圧力を基準とし、酸化剤
ガス側の圧力を燃料ガス側に比して数cmAg程高く維持し
ている。Also, the supply pressure of natural gas reformed gas (H 2 80% + CO 2 20%) as fuel and air as oxidant should be adjusted so that the fuel gas and oxidant gas do not cross-mix through the matrix layer. For example, based on the pressure inside the container, the pressure on the oxidant gas side is kept higher by several cmAg than that on the fuel gas side.
これらの供給ガスに許容される差圧は単電池内のマトリ
ックス層の泡出圧を考慮して定められる。ところで実際
の発電プラントにおいては、燃料電池装置への反応ガス
供給、排出は複雑な配管系と圧力調整弁から成る圧力制
御系を介して行われている。The differential pressure allowed for these supply gases is determined in consideration of the bubble pressure of the matrix layer in the unit cell. By the way, in an actual power plant, the reaction gas is supplied to and discharged from the fuel cell device through a pressure control system including a complicated piping system and a pressure control valve.
これら配管系と燃料電池内反応ガス径路の全径路中最も
耐圧性が小さいのは電解質保持マトリックス層であり、
一方配管系内のガス容量(死容積)が大きく圧力制御系
の応答速度が遅いので、配管系の閉塞や破断等の突然の
事故の場合、特に燃料電池モジュールに近い箇所で行っ
た場合、瞬間に電池内のマトリックス層が破損する可能
性が大であった。It is the electrolyte retention matrix layer that has the lowest pressure resistance among all the paths of these piping systems and the reaction gas path in the fuel cell.
On the other hand, since the gas capacity (dead volume) in the piping system is large and the response speed of the pressure control system is slow, in the case of a sudden accident such as blockage or breakage of the piping system, especially when it is performed near the fuel cell module, Moreover, the matrix layer in the battery was likely to be damaged.
即ち、圧力制御系による差圧制御が行われるまでの瞬間
に燃料ガスが酸化剤ガスかいずれかの圧力が急激に変動
し、マトリックス層で泡出が起こると、このような電解
質層の不可逆的劣化により、この事故以後電解質層で大
巾な交差混合(クロスオーバー)が起こるようになって
しまう。That is, when the pressure of either the fuel gas or the oxidant gas fluctuates rapidly at the moment until the differential pressure control by the pressure control system is performed and bubbles occur in the matrix layer, such irreversible electrolyte layer irreversible Due to deterioration, extensive cross-mixing (crossover) will occur in the electrolyte layer after this accident.
本発明の目的は、供給ガス間の急激な差圧変動が起きた
時、マトリックス層の泡出が起る前に圧力の逃げを生ぜ
しめ、圧力制御系が作動した際元に戻るような圧力逃げ
機構を燃料電池装置内に設けて、マトリックス層の不可
逆的劣化、即ち供給ガスの交差混合の増大を防止するこ
とにある。An object of the present invention is to generate a pressure relief before bubble generation of the matrix layer when a rapid pressure difference variation between supply gases occurs, and to restore the pressure when the pressure control system is activated. The escape mechanism is provided in the fuel cell device to prevent irreversible deterioration of the matrix layer, that is, increase in cross-mixing of the feed gas.
[発明の概要] 本発明は、ガス流路に隣接して設けられる一対の対向す
るガス拡散電極と、このガス拡散電極の間に介在される
電解質を保持したマトリックスとからなる単電池を、セ
パレータを介して複数積層した燃料電池積層体に、前記
ガス流路に反応ガスを供給または排出するための反応ガ
ス供給管または反応ガス排出管を有するマニホールドが
設けられ、これらが圧力容器に収納されてなる燃料電池
装置において、前記マニホールドの内部圧と前記圧力容
器の内部圧との差圧が設定値となるように、該マニホー
ルド内部と該圧力容器内部との間における双方向の圧力
逃げを生ぜしめる圧力逃げ機構と、この圧力逃げ機構を
前記マニホールドに接続するための接続部とを有し、こ
の接続部の断面積が、前記反応ガス供給管または前記反
応ガス排出管の管断面積よりも大きくなるように形成さ
れていることを特徴とする。[Summary of the Invention] The present invention provides a separator comprising a unit cell including a pair of opposed gas diffusion electrodes provided adjacent to a gas flow path, and a matrix holding an electrolyte interposed between the gas diffusion electrodes. A fuel cell stack having a plurality of stacked vias is provided with a manifold having a reaction gas supply pipe or a reaction gas discharge pipe for supplying or discharging a reaction gas to the gas flow path, and these are housed in a pressure vessel. In the fuel cell device, a bidirectional pressure relief is generated between the inside of the manifold and the inside of the pressure container so that the differential pressure between the internal pressure of the manifold and the internal pressure of the pressure container becomes a set value. It has a pressure relief mechanism and a connection portion for connecting the pressure relief mechanism to the manifold, and the cross-sectional area of the connection portion is the reaction gas supply pipe or the reaction gas. It is characterized in that it is formed to be larger than the cross-sectional area of the gas discharge pipe.
[発明の効果] 本発明のように圧力逃げ機構をマニホールドに接続する
ことにより、マニホールド内の圧力が圧力容器内の圧力
に比較して設定値よりも上昇或いは下降することがなく
なり、配管系の閉塞、破壊等による事故により、圧力制
御系が復帰するまでの間電池内圧力の急激上昇時におけ
る単電池のマトリックス層破壊を防止することができ
る。[Effects of the Invention] By connecting the pressure relief mechanism to the manifold as in the present invention, the pressure in the manifold does not rise or fall below the set value as compared with the pressure in the pressure vessel, and the piping system It is possible to prevent the matrix layer from being destroyed in the unit cell when the internal pressure of the cell is rapidly increased until the pressure control system is restored due to an accident such as blockage or destruction.
また、圧力逃げ機構とマニホールドとの接続部の断面積
を反応ガス供給管または反応ガス排出管の管断面積より
も大きくなるように形成することにより、圧力急変時の
応答速度が速くなり、マトリックス層の泡出が起きる前
に確実に圧力逃げを生ぜしめることが可能となり、燃料
電池装置としての信頼性を著しく向上させることができ
る。Further, by forming the cross-sectional area of the connection portion between the pressure relief mechanism and the manifold to be larger than the cross-sectional area of the reaction gas supply pipe or the reaction gas discharge pipe, the response speed at the time of sudden pressure change becomes faster, and the matrix It is possible to surely generate the pressure relief before the layer bubbles, and it is possible to remarkably improve the reliability of the fuel cell device.
なお本発明は第一世代型に限定されるものではなく、第
二世代型の溶融炭酸塩燃料電池にも同様に適用できる。
この際には液封のための液体として炭酸リチウムと炭酸
カリウムの共融組成の溶融塩等が使用される。The present invention is not limited to the first generation type, but can be similarly applied to the second generation type molten carbonate fuel cell.
At this time, a molten salt having a eutectic composition of lithium carbonate and potassium carbonate is used as a liquid for liquid sealing.
以下本発明の実施例を図面に基づいて詳細に説明する。 Embodiments of the present invention will be described in detail below with reference to the drawings.
第3図は本発明の一実施例として圧力逃げ機構31として
レリーフバルブを用いたものの構造の一例を示したもの
である。マニホールド10からでる接続管11に取り付けた
円筒形のシリンダ13内に設定基準圧に対応するバネ定数
を有するスプリン14及び14′を入れ、その間にガス流路
を設けた弁15を介在させる。適当なバネ定数のスプリン
グを選定することにより、マニホールド10内の圧力が高
まり、マトリックスの泡圧力に近づいた時、可動弁15が
移動して溝15aとガス排出管17が連絡され、ここを通し
てガスは圧力容器12内に排出される。逆にマニホールド
10内の圧力が低くなると圧力容器12内の不活性ガスがガ
ス排出管17、可動弁15を通ってマニホールド内に流れ込
む。このようなレリーフバルブを例えば第2図の各マニ
ホールド10a,10b,10c,10dからとり出した接続管11a,11
b,11c,11dに接続することにより、マニホールド内の圧
力が基準値以上に上昇、或いは下降するのを防止でき
る。即ち設定差圧以内にとどめておくことができる。
又、設定差圧以内ではガスの連絡がない。FIG. 3 shows an example of the structure of a structure using a relief valve as the pressure relief mechanism 31 as one embodiment of the present invention. Splines 14 and 14 'having a spring constant corresponding to a set reference pressure are placed in a cylindrical cylinder 13 attached to a connecting pipe 11 extending from a manifold 10, and a valve 15 provided with a gas flow path is interposed therebetween. By selecting a spring with an appropriate spring constant, when the pressure inside the manifold 10 rises and approaches the bubble pressure in the matrix, the movable valve 15 moves and the groove 15a and the gas discharge pipe 17 are communicated with each other. Is discharged into the pressure vessel 12. Conversely the manifold
When the pressure in 10 decreases, the inert gas in the pressure vessel 12 flows into the manifold through the gas discharge pipe 17 and the movable valve 15. Such relief valves are, for example, connecting pipes 11a, 11 taken out from the respective manifolds 10a, 10b, 10c, 10d of FIG.
By connecting to b, 11c and 11d, it is possible to prevent the pressure in the manifold from rising or falling above the reference value. That is, it can be kept within the set differential pressure.
Also, there is no gas communication within the set differential pressure.
上述のばね式のレリーフバルブの換わりに第4図,第5
図のような液封機構の双方向性圧力逃げ機構31′,31″
を用いることもできる。4 and 5 instead of the spring type relief valve described above.
Bi-directional pressure relief mechanism 31 ′, 31 ″ of liquid sealing mechanism as shown
Can also be used.
第4図はこのような弁の構造をその断面図で示したもの
である。マニホールド10の上部に図示の構造を有する液
溜め18,19を設けた一端がマニホールド10に取着けら
れ、他端が圧力容器12内に開放した曲管29,30がとりつ
けてあり、この液溜め18,19には気密を維持するため適
当な比重、粘度の高沸点油20を満たし、ここに適当な重
量例えば5〜10g/cm2の浮き21,22を置いてある。FIG. 4 is a sectional view showing the structure of such a valve. The liquid reservoirs 18, 19 having the structure shown in the figure are provided on the upper part of the manifold 10, one end is attached to the manifold 10, and the other end is provided with open curved pipes 29, 30 in the pressure vessel 12. In order to maintain airtightness, 18, 19 are filled with high boiling point oil 20 having an appropriate specific gravity and viscosity, and floats 21, 22 having an appropriate weight, for example, 5-10 g / cm 2 are placed there.
今、マニホールド内の圧力が圧力容器より上がった時、
ガスは図中の実線Aで示した経路を流れ、浮き21を持ち
上げ、圧力容器12内に排出される。逆にマニホールド内
の圧力が圧力容器より設安差圧以上下がった時、ガスは
図中の破線Bの経路を流れ、浮き22を持ち上げマニホー
ルド内に侵入していく。マニホールド内の圧力と圧力容
器内の圧力の差圧が設定圧に保たれている時は双方の浮
き21,22は下がっており、両者間のガスの気密は保持さ
れる。Now when the pressure in the manifold rises above the pressure vessel,
The gas flows through the path shown by the solid line A in the figure, lifts the float 21, and is discharged into the pressure vessel 12. Conversely, when the pressure in the manifold falls below the pressure drop of the pressure vessel by a pressure equal to or greater than the set pressure difference, the gas flows through the path indicated by the broken line B in the figure, lifts the float 22, and enters the manifold. When the pressure difference between the pressure inside the manifold and the pressure inside the pressure vessel is maintained at the set pressure, the floats 21 and 22 on both sides are lowered, and the airtightness of the gas between them is maintained.
第5図は、同様な液封機構の双方向性の弁の他の例を示
したものである。FIG. 5 shows another example of a bidirectional valve having a similar liquid sealing mechanism.
マニホールド10に液溜めのための凹部23,24を設け、こ
こに高沸点の油20を満たし、ここに適当な形状で一定の
比重を有する浮き25,26を置く、又凹部の上部には、系
内の圧力上昇で浮きが上昇した時飛んでしまうのを防止
するためのツメ27,28をつけておく。マニホールド内の
圧力が設定値以上に上昇した時、浮き25が上昇し、ガス
は圧力容器内に逃げる。逆にマニホールド内の圧力が圧
力容器に較べ設定値以上低下した時浮き26が上昇して圧
力容器内の不活性ガスがマニホールド内に逃げる。両者
間の差圧が一定値に保たれている時、双方の浮き25,26
は落ちてマニホールドと圧力容器間の差圧は一定に保た
れている。The manifold 10 is provided with recesses 23, 24 for storing liquid, the high boiling point oil 20 is filled therein, and the floats 25, 26 having an appropriate shape and constant specific gravity are placed therein, and the upper part of the recess is Claws 27 and 28 are attached to prevent flying when the float rises due to pressure increase in the system. When the pressure in the manifold rises above the set value, the float 25 rises and the gas escapes into the pressure vessel. On the contrary, when the pressure in the manifold is lower than the pressure vessel by a set value or more, the float 26 rises and the inert gas in the pressure vessel escapes into the manifold. When the pressure difference between the two is kept constant, the
The pressure drop between the manifold and the pressure vessel is kept constant.
上述の双方向性の弁は構造が簡単で、しかもガスの逃げ
る面積が大きくとれるので圧力急変時の応答速度が速く
なり有利となる。The bidirectional valve described above is simple in structure and has a large gas escape area. Therefore, the response speed at the time of a sudden pressure change is fast, which is advantageous.
上記第3図,第4図の構造においても、圧力急変時の応
答速度を速くするために、マニホールドに取り付ける部
分の管径をガス供給、排出管の管径よりも太くなるよう
にする。即ち、接続管の管断面積が、ガス供給、排出管
の管断面積よりも大きくなるように形成されている。か
かる構成によれば、供給ガス間に急激な差圧変動が起き
た場合でも、マトリックス層の泡出が起きる前に確実に
圧力逃げを生じさせることが可能となる。Also in the structures shown in FIGS. 3 and 4, the pipe diameter of the portion attached to the manifold is made larger than the pipe diameters of the gas supply and discharge pipes in order to increase the response speed when the pressure changes abruptly. That is, the pipe cross-sectional area of the connecting pipe is formed to be larger than the pipe cross-sectional areas of the gas supply and discharge pipes. According to such a configuration, even if a sudden difference in pressure difference occurs between the supply gases, it becomes possible to surely cause the pressure escape before the foaming of the matrix layer occurs.
上記第5図の構造の圧力逃げ機構において、圧力逃げの
部分の数は1個に限らず、各取り付け部分の浮きの重さ
は少しずつ変えておいても良い。又液封に用いる油は常
温で固体であっても良い。In the pressure relief mechanism having the structure of FIG. 5 described above, the number of pressure relief portions is not limited to one, and the weight of floating at each mounting portion may be slightly changed. The oil used for liquid sealing may be solid at room temperature.
第1図は燃料電池の発電ユニットを説明する為に示す
図、第2図は燃料電池スタックの概略を示す図、第3図
は本発明に係る一実施例の要部を示す断面図、第4図,
第5図は本発明の他の実施例を示す断面図である。 10……マニホールド、1……接続管、13……シリンダ、
14,14′……スプリング、15……弁、17……ガス排出
管、31……圧力逃げ機構。FIG. 1 is a diagram for explaining a power generation unit of a fuel cell, FIG. 2 is a diagram showing an outline of a fuel cell stack, and FIG. 3 is a sectional view showing an essential part of an embodiment according to the present invention. Figure 4,
FIG. 5 is a sectional view showing another embodiment of the present invention. 10 …… manifold, 1 …… connection pipe, 13 …… cylinder,
14,14 ′ …… Spring, 15 …… Valve, 17 …… Gas discharge pipe, 31 …… Pressure relief mechanism.
Claims (1)
するガス拡散電極と、このガス拡散電極の間に介在され
る電解質を保持したマトリックスとからなる単電池を、
セパレータを介して複数積層した燃料電池積層体に、前
記ガス流路に反応ガスを供給または排出するための反応
ガス供給管または反応ガス排出管を有するマニホールド
が設けられ、これらが圧力容器に収納されてなる燃料電
池装置において、 前記マニホールドの内部圧と前記圧力容器の内部圧との
差圧が設定値となるように、該マニホールド内部と該圧
力容器内部との間における双方向の圧力逃げを生ぜしめ
る圧力逃げ機構と、この圧力逃げ機構を前記マニホール
ドに接続するための接続部とを有し、この接続部の断面
積が、前記反応ガス供給管または前記反応ガス排出管の
管断面積よりも大きくなるように形成されていることを
特徴とする燃料電池装置。1. A unit cell comprising a pair of opposed gas diffusion electrodes provided adjacent to a gas flow path, and a matrix holding an electrolyte interposed between the gas diffusion electrodes,
A plurality of fuel cell stacks with a separator interposed therebetween is provided with a manifold having a reaction gas supply pipe or a reaction gas discharge pipe for supplying or discharging a reaction gas to the gas flow path, and these are housed in a pressure vessel. In the fuel cell device, a bidirectional pressure relief is generated between the inside of the manifold and the inside of the pressure vessel so that the differential pressure between the internal pressure of the manifold and the internal pressure of the pressure vessel becomes a set value. A pressure relief mechanism for tightening, and a connection portion for connecting the pressure relief mechanism to the manifold, and the cross-sectional area of this connection portion is larger than the cross-sectional area of the reaction gas supply pipe or the reaction gas discharge pipe. A fuel cell device, which is formed to be large.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58240997A JPH0754711B2 (en) | 1983-12-22 | 1983-12-22 | Fuel cell device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58240997A JPH0754711B2 (en) | 1983-12-22 | 1983-12-22 | Fuel cell device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60133666A JPS60133666A (en) | 1985-07-16 |
| JPH0754711B2 true JPH0754711B2 (en) | 1995-06-07 |
Family
ID=17067786
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58240997A Expired - Lifetime JPH0754711B2 (en) | 1983-12-22 | 1983-12-22 | Fuel cell device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0754711B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE10010394A1 (en) * | 2000-02-28 | 2001-09-06 | Mannesmann Ag | Fuel cell used in the automobile industry has pressure regulators arranged in both removal lines of the anode and cathode parts. |
| KR100633692B1 (en) | 2005-11-03 | 2006-10-11 | 주식회사 만도 | Relief Valve and Shock Absorber Using the Same |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58165269A (en) * | 1982-03-26 | 1983-09-30 | Fuji Electric Corp Res & Dev Ltd | Pressure controller of supply gas to fuel cell |
-
1983
- 1983-12-22 JP JP58240997A patent/JPH0754711B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60133666A (en) | 1985-07-16 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US7517608B2 (en) | Inherently safe redox flow battery storage system | |
| US4833046A (en) | Metal-hydrogen secondary battery | |
| US12068513B2 (en) | Sealed redox battery | |
| KR850002699A (en) | Liquid fuel cell | |
| EP0177225A1 (en) | Active cooling system for electrochemical cells | |
| US20030198862A1 (en) | Liquid gallium alkaline electrolyte fuel cell | |
| CA2269382C (en) | Electrode assembly | |
| EP0672307B1 (en) | Method and apparatus for charging and discharging electric energy | |
| US3839091A (en) | Regenerative fuel cell | |
| CN101425590A (en) | Hydrogen gas security protection system for fuel cell engine | |
| US4513066A (en) | Thin-film, high pressure fuel cell | |
| CN117779076A (en) | Methods and equipment for preparing one or more electrolytic products | |
| JPH0754711B2 (en) | Fuel cell device | |
| CN100361334C (en) | A fuel cell power generation system with a hydrogen intermittent safety discharge device | |
| US4012234A (en) | Water activation and pressure equalization of electrochemical batteries | |
| JP2025517445A (en) | Passive Dual Modulation Regulator for Hydrogen Generation | |
| CN100361336C (en) | A high-pressure hydrogen storage device in a fuel cell power generation system | |
| Abbey et al. | Pore size engineering applied to starved electrochemical cells and batteries | |
| US3540932A (en) | Method of supplying gas in liquid electrolyte to electrochemical cell | |
| CN115295851B (en) | Flow battery systems and their applications | |
| JPS6188464A (en) | Fuel cell | |
| JPS60124367A (en) | Electrolyte circulation system of fuel cell | |
| CN210778821U (en) | Rechargeable sodium-water gas fuel cell unit | |
| Jones et al. | Nickel hydrogen common pressure vessel battery development | |
| JPS626309B2 (en) |