JP3258378B2 - Fuel cell - Google Patents

Fuel cell

Info

Publication number
JP3258378B2
JP3258378B2 JP17574892A JP17574892A JP3258378B2 JP 3258378 B2 JP3258378 B2 JP 3258378B2 JP 17574892 A JP17574892 A JP 17574892A JP 17574892 A JP17574892 A JP 17574892A JP 3258378 B2 JP3258378 B2 JP 3258378B2
Authority
JP
Japan
Prior art keywords
gas supply
cooling water
fuel cell
fuel
separator
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
Application number
JP17574892A
Other languages
Japanese (ja)
Other versions
JPH0620713A (en
Inventor
俊宏 谷
長生 久留
聡 内田
穰 末田
勇夫 平田
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 Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
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 Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP17574892A priority Critical patent/JP3258378B2/en
Publication of JPH0620713A publication Critical patent/JPH0620713A/en
Application granted granted Critical
Publication of JP3258378B2 publication Critical patent/JP3258378B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04082Arrangements for control of reactant parameters, e.g. pressure or concentration
    • H01M8/04089Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
    • 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
    • H01M8/2465Details of groupings of fuel cells
    • H01M8/2483Details of groupings of fuel cells characterised by internal manifolds
    • 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
    • H01M8/0202Collectors; 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
    • H01M8/026Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant characterised by grooves, e.g. their pitch or depth
    • 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
    • H01M8/0267Collectors; Separators, e.g. bipolar separators; Interconnectors having heating or cooling means, e.g. heaters or coolant flow channels
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00Electrolytes
    • H01M2300/0017Non-aqueous electrolytes
    • H01M2300/0065Solid electrolytes
    • H01M2300/0082Organic polymers
    • 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

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】この発明は、固体高分子膜を使用
した燃料電池の改良に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an improvement in a fuel cell using a solid polymer membrane.

【0002】[0002]

【従来の技術】従来、燃料電池の燃料ガスと酸化剤ガス
はマニホールド構造により供給されていたため、直交し
ていた。また、内部ヘッダー方式をとり燃料ガスと酸化
剤ガスが平行流が可能となるセパレータを使用した例
(特願平3−154558)もあるが、その実施例から
もわかるようにガス流れ方向が重力方向下方として冷却
水が滞ることなく循環するものは無かった。
2. Description of the Related Art Conventionally, a fuel gas and an oxidizing gas of a fuel cell have been supplied orthogonally because of a manifold structure. There is also an example in which an internal header system is employed and a fuel gas and an oxidizing gas are allowed to flow in parallel (Japanese Patent Application No. 3-154558). However, as can be seen from this embodiment, the gas flow direction is gravity. There was no cooling water circulating without stagnating downward.

【0003】[0003]

【発明が解決しようとする課題】ところで、固体高分子
膜を電解質として利用する場合、十分に含水していなけ
れば電解質として高い性能を発揮できないものが多い。
例えば、プロトン伝導体であるナフィオン(デュポン
製)などがその典型である。これらの固体高分子膜を用
いて燃料電池を構成する場合、膜に水に供給する方法と
して、燃料としてまた酸化剤として導入されるガスの片
方もしくは両方を加湿する方法がとられている。
When a solid polymer membrane is used as an electrolyte, many electrolytes cannot exhibit high performance unless they contain sufficient water.
For example, Nafion (produced by DuPont), which is a proton conductor, is a typical example. When a fuel cell is formed using these solid polymer membranes, a method of supplying one or both of gases introduced as a fuel and an oxidant is used as a method for supplying water to the membrane.

【0004】しかしながら、燃料電池の運転条件によっ
ては、水分がセパレータの表面にドレンとなってしまう
ことがある。セパレータの表面にはガス供給用の細い溝
があるが、この細い溝がドレンで被われてしまうとガス
供給が不可能となり、性能が著しく低下してしまう。
[0004] However, depending on the operating conditions of the fuel cell, water may drain on the surface of the separator. Although there is a thin groove for gas supply on the surface of the separator, if this narrow groove is covered with drain, gas supply becomes impossible and the performance is remarkably deteriorated.

【0005】従来のセパレータでは、このような状況を
考慮しておらず、水分がセパレータの表面に付着するよ
うな条件で運転するためには、ガス利用率を落とし、排
気ガスを増やし、そのガス流れによってドレンを取り去
らなければならなかった。
In the conventional separator, such a situation is not taken into consideration, and in order to operate under conditions where moisture adheres to the surface of the separator, the gas utilization rate is reduced, the exhaust gas is increased, and the The drain had to be removed by the flow.

【0006】この発明はこうした事情を考慮してなされ
たもので、セパレータにある燃料ガス供給用溝及び酸化
剤ガス供給用溝を平行流とするとともに、その流れ方向
を重力方向下方としてドレンと排出される構造とするこ
とにより、ガス利用率を落とすことなく種々な条件で運
転しえる燃料電池を提供することを目的とする。
The present invention has been made in view of such circumstances, and the fuel gas supply groove and the oxidizing gas supply groove in the separator are made to flow in parallel, and the flow direction is made lower in the direction of gravity to drain and discharge. It is an object of the present invention to provide a fuel cell that can be operated under various conditions without lowering the gas utilization rate.

【0007】[0007]

【課題を解決するための手段】この発明は、固体電解質
膜としての固体高分子膜の両面に酸化剤極と燃料極を設
けた燃料電池セルと、この燃料電池セルの両側に夫々設
けられたセパレータとを具備し、前記セパレータは、片
面に端部付近まで達する酸化剤ガス供給用溝を形成した
酸化剤ガス供給板と、片面に前記酸化剤ガス供給用溝と
平行で実質的に同一長さであるとともに端部付近まで達
する燃料ガス供給用溝を形成した燃料ガス供給板と、前
記両ガス供給板間に配置されて,前記燃料電池セルと非
接触の状態で冷却水用溝を形成した冷却水板とから構成
され、前記セパレータの下部に冷却水供給孔を設けると
ともに、この冷却水供給孔より上側に位置する前記セパ
レータに冷却水排水孔を設け、燃料ガス及び酸化剤ガス
が夫々前記燃料ガス供給用溝,酸化剤ガス供給用溝内を
重力方向に自然に排出されるとともに、冷却水が前記セ
パレータの下部から供給された後,冷却水用溝を経て冷
却水排水孔から排出される構成であることを特徴とする
燃料電池である。
According to the present invention, there is provided a fuel cell in which an oxidizer electrode and a fuel electrode are provided on both sides of a solid polymer membrane as a solid electrolyte membrane, and a fuel cell provided on both sides of the fuel cell. A separator, wherein the separator is formed on one side with an oxidizing gas supply plate formed with an oxidizing gas supply groove reaching the vicinity of the end , and on one side is substantially the same length as the oxidizing gas supply groove. It is near the end
A fuel gas supply plate having a fuel gas supply groove formed therein, and a cooling water plate disposed between the two gas supply plates and having a cooling water groove formed in a non-contact state with the fuel cell. A cooling water supply hole provided in a lower portion of the separator, and a cooling water drain hole provided in the separator positioned above the cooling water supply hole, so that a fuel gas and an oxidizing gas are respectively supplied to the fuel gas supply hole. And the cooling water is supplied from the lower part of the separator and then discharged from the cooling water drain hole through the cooling water groove. There is provided a fuel cell.

【0008】[0008]

【作用】この発明においては、セパレータの両面に互い
に平行な燃料ガス供給用溝及び酸化剤ガス供給用溝を設
け、かつ燃料ガス及び酸化剤ガスが前記溝内を重力方向
(垂直方向)の下方に自然に排出される構成になってお
いるため、ガス利用率を落とすことなく、様々な条件で
運転することができる。
According to the present invention, a fuel gas supply groove and an oxidant gas supply groove which are parallel to each other are provided on both surfaces of the separator, and the fuel gas and the oxidant gas flow downward in the direction of gravity (vertical direction) in the groove. Because it is configured to be discharged naturally, it can be operated under various conditions without lowering the gas utilization rate.

【0009】[0009]

【実施例】以下、この発明の実施例を図を参照して説明
する。 (実施例1)図1を参照する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings. Embodiment 1 Referring to FIG.

【0010】図中の1は、燃料電池発電体(セル)を示
す。この燃料電池セル1は、電解質膜としての固体高分
子膜と、この固体高分子膜の両面に酸化剤極2,燃料極
3とを貼り付けた構成になっている。前記燃料電池セル
1の左右には、パッキン4が取り付けられている。
Reference numeral 1 in the drawing denotes a fuel cell power generator (cell). The fuel cell 1 has a configuration in which a solid polymer membrane as an electrolyte membrane and an oxidizer electrode 2 and a fuel electrode 3 are attached to both surfaces of the solid polymer membrane. Packings 4 are attached to the left and right of the fuel cell 1.

【0011】前記燃料電池セル1及びパッキン4の両主
面側は、セパレータ5によって挟み付けられている。こ
のセパレータ5の上部隅の一方側には燃料ガス供給孔6
が設けられ、下部隅の一方側には燃料ガス排出孔7が設
けられ、更にセパレータ5の一方の主面の中央部には燃
料ガス供給溝8が上下方向に設けられている。また、セ
パレータ5の上部隅の他方側には酸化剤ガス供給孔9が
設けられ、下部隅の他方側には酸化剤ガス排出孔10が
設けられ、更にセパレータ5の他方の主面の中央部には
酸化剤ガス供給溝11が上下方向に設けられている。こ
こで、前記燃料ガス供給溝8と酸化剤ガス供給溝11は
平行に形成されている。なお、図中の1aはセル端部シ
ールを示す。
The two main surfaces of the fuel cell 1 and the packing 4 are sandwiched between separators 5. One side of the upper corner of the separator 5 is provided with a fuel gas supply hole 6.
A fuel gas discharge hole 7 is provided on one side of the lower corner, and a fuel gas supply groove 8 is provided in the center of one main surface of the separator 5 in the vertical direction . An oxidizing gas supply hole 9 is provided on the other side of the upper corner of the separator 5, an oxidizing gas discharge hole 10 is provided on the other side of the lower corner, and a central portion of the other main surface of the separator 5 is provided. Is provided with an oxidizing gas supply groove 11 in a vertical direction. Here, the fuel gas supply groove 8 and the oxidizing gas supply groove 11 are formed in parallel. Incidentally, reference numeral 1a in the drawing denotes a cell end seal.

【0012】こうした構成の燃料電池において、前記燃
料ガス供給孔6より導入された燃料ガス(水素)は、セ
パレータ5内部に設けられたヘッダーからセパレータ表
面の燃料ガス供給溝8を通じて燃料電池セル1の燃料極
側3側に供給される。一方、酸化剤ガス(空気)は、酸
化剤ガス供給孔9より導入され、燃料ガスと裏面同士の
経路を通り燃料電池セル1の酸化剤極2側に供給され
る。
In the fuel cell having such a configuration, the fuel gas (hydrogen) introduced from the fuel gas supply hole 6 is supplied from the header provided inside the separator 5 to the fuel cell 1 through the fuel gas supply groove 8 on the separator surface. The fuel is supplied to the fuel electrode 3 side. On the other hand, the oxidant gas (air) is introduced from the oxidant gas supply hole 9 and supplied to the oxidant electrode 2 side of the fuel cell 1 through the path between the fuel gas and the back surface.

【0013】このように、上記実施例1に係る燃料電池
によれば、固体電解質膜としての固体高分子膜の両面に
酸化剤極2と燃料極3を設けた燃料電池セル1と、この
燃料電池セル1の両側に夫々設けられたセパレータ5と
を有し、前記セパレータ5の両面に互いに平行な燃料ガ
ス供給用溝8及び酸化剤ガス供給用溝11を設け、かつ燃
料ガス及び酸化剤が前記溝内を重力方向下方に自然に排
出される構成になっているため、ガス利用率の大幅な向
上と様々な運転条件でも十分な発電性能を得ることがで
きる。特に、ガス利用率では、酸化剤ガス(空気中酸
素)の利用率を70%以上にすることが可能となった。ま
た、燃料電池へ導入する以前のガスの含湿率を燃料電池
セル以上の温度の飽和蒸気相当として運転し、燃料電池
内にドレンが発生する状況であっても連続で発電可能で
ある。 (実施例2)
As described above, according to the fuel cell of the first embodiment, the fuel cell 1 in which the oxidizer electrode 2 and the fuel electrode 3 are provided on both surfaces of the solid polymer membrane as the solid electrolyte membrane, A separator 5 provided on both sides of the battery cell 1; a fuel gas supply groove 8 and an oxidant gas supply groove 11 which are parallel to each other on both surfaces of the separator 5; Since it is configured to be naturally discharged downward in the direction of gravity in the groove, it is possible to greatly improve the gas utilization rate and obtain sufficient power generation performance even under various operating conditions. In particular, the utilization rate of the oxidizing gas (oxygen in the air) can be increased to 70% or more. Further, the operation is performed with the moisture content of the gas before being introduced into the fuel cell being equivalent to the saturated vapor at a temperature equal to or higher than that of the fuel cell, and continuous power generation is possible even in a situation where drainage occurs in the fuel cell. (Example 2)

【0014】図2、図3を参照する。ここで、図2は実
施例2に係る燃料電池の説明図、図3は図2の燃料電池
の一構成であるセパレータの分解斜視図を示す。なお、
図1と同部材は同符号を付して説明を省略する。
Please refer to FIG. 2 and FIG. Here, FIG. 2 is an explanatory view of the fuel cell according to the second embodiment, and FIG. 3 is an exploded perspective view of a separator which is one configuration of the fuel cell of FIG. In addition,
1 are denoted by the same reference numerals and description thereof is omitted.

【0015】実施例2は、冷却水をセパレータ内に流す
方法をとる実施例である。セパレータ5は、燃料ガス供
給板21と、酸化剤ガス供給板22と、これらの両供給板間
に挟まれた冷却水板23とから構成されている。前記セパ
レータ5の下部には冷却水供給孔24が形成され、セパレ
ータ5の上部には冷却水排水孔25が形成されている。冷
却水板23には、冷却水供給孔24と冷却水排水孔25とを連
通する冷却水供給溝26が形成されている。前記酸化剤ガ
ス供給板22には、冷却水供給孔24に連通する冷却水供給
ヘッダ27、及び前記冷却水排水孔25に連通する冷却水排
出ヘッダ28がそれぞれ形成されている。前記酸化剤ガス
供給板22には、酸化剤ガス供給孔9に連通する酸化剤ガ
ス供給ヘッダ29、及び前記酸化剤ガス排出孔10に連通す
る酸化剤ガス排出ヘッダ30がそれぞれ形成されている。
Embodiment 2 is an embodiment in which a method of flowing cooling water into a separator is employed. The separator 5 includes a fuel gas supply plate 21, an oxidizing gas supply plate 22, and a cooling water plate 23 interposed between these two supply plates. A cooling water supply hole 24 is formed at a lower portion of the separator 5, and a cooling water drain hole 25 is formed at an upper portion of the separator 5. The cooling water plate 23 is formed with a cooling water supply groove 26 that connects the cooling water supply hole 24 and the cooling water drain hole 25. On the oxidizing gas supply plate 22, a cooling water supply header 27 communicating with the cooling water supply hole 24 and a cooling water discharge header 28 communicating with the cooling water drain hole 25 are formed. The oxidizing gas supply plate 22 is formed with an oxidizing gas supply header 29 communicating with the oxidizing gas supply hole 9 and an oxidizing gas discharge header 30 communicating with the oxidizing gas discharge hole 10.

【0016】こうした構成の燃料電池において、冷却水
はセパレータ下部にある冷却水供給孔24より入り、冷却
水板23に設けられた冷却水供給溝26を通り、セパレータ
上部の冷却水排水孔25より排出される。しかして、図3
に示すセパレータを用いることにより、燃料ガス,酸化
剤ガスの両方ともガス供給溝を上方から下方へ流れ、か
つ冷却水は空気溜り等をつくることなく、スムーズに流
すことができる。
In the fuel cell having such a configuration, the cooling water enters through the cooling water supply hole 24 provided at the lower part of the separator, passes through the cooling water supply groove 26 provided on the cooling water plate 23, and flows through the cooling water drain hole 25 provided at the upper part of the separator. Is discharged. Thus, FIG.
By using the separator shown in (1), both the fuel gas and the oxidizing gas flow from the upper side to the lower side in the gas supply groove, and the cooling water can flow smoothly without forming an air pocket or the like.

【0017】なお、上記実施例では、燃料電池が1つの
燃料電池セルとこのセルの両側のセパレータから構成さ
れる場合について述べたが、これに限らず、燃料電池セ
ルとセパレータを交互に多数積層した構成のものでもよ
い。
In the above embodiment, the case where the fuel cell is composed of one fuel cell and the separators on both sides of the cell has been described. However, the present invention is not limited to this, and a large number of fuel cells and separators are alternately stacked. The configuration may be as follows.

【0018】[0018]

【発明の効果】以上詳述したようにこの発明によれば、
セパレータにある燃料ガス供給用溝及び酸化剤ガス供給
用溝を平行流とするとともに、その流れ方向を重力方向
の下方としてドレンと排出される構造とすることによ
り、ガス利用率を落とすことなく種々な条件で運転しえ
る燃料電池を提供できる。
As described in detail above, according to the present invention,
The fuel gas supply groove and the oxidizing gas supply groove in the separator are made to flow in parallel, and the flow direction is downward in the direction of gravity, and the structure is configured to be discharged with drain so that the gas utilization rate can be reduced without decreasing the gas utilization rate. A fuel cell that can be operated under various conditions can be provided.

【図面の簡単な説明】[Brief description of the drawings]

【図1】この発明の実施例1に係る燃料電池の説明図。FIG. 1 is an explanatory diagram of a fuel cell according to Embodiment 1 of the present invention.

【図2】この発明の実施例2に係る燃料電池の説明図。FIG. 2 is an explanatory view of a fuel cell according to Embodiment 2 of the present invention.

【図3】図2の燃料電池の一構成であるセパレータの分
解斜視図。
FIG. 3 is an exploded perspective view of a separator which is one configuration of the fuel cell of FIG. 2;

【符号の説明】[Explanation of symbols]

1…燃料電池セル、2…酸化剤極、3…燃料極、4…パ
ッキング、5…セパレータ、6…燃料ガス供給孔、7…
燃料ガス排出孔、8…燃料ガス供給溝、9…酸化剤ガス
供給孔、10…酸化剤ガス排出孔、21…冷却水供給板、22
…酸化剤ガス供給板、24…冷却水供給孔、25…冷却水排
水孔、26…冷却水供給溝、27…冷却水供給ヘッダ、28…
冷却水排出ヘッダ28。
DESCRIPTION OF SYMBOLS 1 ... Fuel cell, 2 ... Oxidizer electrode, 3 ... Fuel electrode, 4 ... Packing, 5 ... Separator, 6 ... Fuel gas supply hole, 7 ...
Fuel gas discharge hole, 8: fuel gas supply groove, 9: oxidant gas supply hole, 10: oxidant gas discharge hole, 21: cooling water supply plate, 22
... Oxidant gas supply plate, 24 ... Cooling water supply hole, 25 ... Cooling water drain hole, 26 ... Cooling water supply groove, 27 ... Cooling water supply header, 28 ...
Cooling water discharge header 28.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 末田 穰 広島県広島市西区観音新町四丁目6番22 号 三菱重工業株式会社広島研究所内 (72)発明者 平田 勇夫 広島県広島市西区観音新町四丁目6番22 号 三菱重工業株式会社広島研究所内 (56)参考文献 特開 昭60−163375(JP,A) 特開 昭60−236459(JP,A) 特開 平3−102774(JP,A) 特開 平4−267062(JP,A) (58)調査した分野(Int.Cl.7,DB名) H01M 8/02 H01M 8/04 H01M 8/10 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Joi Sueda 4--22 Kannon Shinmachi, Nishi-ku, Hiroshima, Hiroshima Prefecture Inside the Hiroshima Research Laboratory, Mitsubishi Heavy Industries, Ltd. (72) Inventor Isao Hirata 4-chome, Kannon Shinmachi, Nishi-ku, Hiroshima, Hiroshima Prefecture No. 6-22 Inside Mitsubishi Heavy Industries, Ltd. Hiroshima Laboratory (56) References JP-A-60-163375 (JP, A) JP-A-60-236459 (JP, A) JP-A-3-102774 (JP, A) Kaihei 4-266706 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) H01M 8/02 H01M 8/04 H01M 8/10

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 固体電解質膜としての固体高分子膜の両
面に酸化剤極と燃料極を設けた燃料電池セルと、この燃
料電池セルの両側に夫々設けられたセパレータとを具備
し、 前記セパレータは、片面に端部付近まで達する酸化剤ガ
ス供給用溝を形成した酸化剤ガス供給板と、片面に前記
酸化剤ガス供給用溝と平行で実質的に同一長さであると
ともに端部付近まで達する燃料ガス供給用溝を形成した
燃料ガス供給板と、前記両ガス供給板間に配置されて,
前記燃料電池セルと非接触の状態で冷却水用溝を形成し
た冷却水板とから構成され、 前記セパレータの下部に冷却水供給孔を設けるととも
に、この冷却水供給孔より上側に位置する前記セパレー
タに冷却水排水孔を設け、 燃料ガス及び酸化剤ガスが夫々前記燃料ガス供給用溝,
酸化剤ガス供給用溝内を重力方向に自然に排出されると
ともに、冷却水が前記セパレータの下部から供給された
後,冷却水用溝を経て冷却水排水孔から排出される構成
であることを特徴とする燃料電池。
1. A fuel cell comprising an oxidant electrode and a fuel electrode provided on both sides of a solid polymer film as a solid electrolyte membrane, and separators provided on both sides of the fuel cell, respectively. Is an oxidizing gas supply plate formed with an oxidizing gas supply groove reaching one end near the end, and is substantially the same length as the oxidizing gas supply groove on one surface being parallel to the oxidizing gas supply groove.
A fuel gas supply plate formed with a fuel gas supply groove both reaching near the end, and a fuel gas supply plate disposed between the two gas supply plates;
A cooling water plate formed with a cooling water groove in a non-contact state with the fuel cell unit, wherein a cooling water supply hole is provided at a lower portion of the separator, and the separator is located above the cooling water supply hole. Cooling water drain holes are provided in the fuel gas supply grooves and the oxidizing gas , respectively.
The structure is such that the oxidizing gas supply groove is naturally discharged in the direction of gravity in the gravity direction, and the cooling water is supplied from the lower part of the separator and then discharged from the cooling water drain hole through the cooling water groove. Features fuel cell.
JP17574892A 1992-07-02 1992-07-02 Fuel cell Expired - Lifetime JP3258378B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17574892A JP3258378B2 (en) 1992-07-02 1992-07-02 Fuel cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17574892A JP3258378B2 (en) 1992-07-02 1992-07-02 Fuel cell

Publications (2)

Publication Number Publication Date
JPH0620713A JPH0620713A (en) 1994-01-28
JP3258378B2 true JP3258378B2 (en) 2002-02-18

Family

ID=16001566

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17574892A Expired - Lifetime JP3258378B2 (en) 1992-07-02 1992-07-02 Fuel cell

Country Status (1)

Country Link
JP (1) JP3258378B2 (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0833400B1 (en) * 1995-05-25 2005-08-03 Honda Giken Kogyo Kabushiki Kaisha Fuel cell and method for its control
JP3505010B2 (en) 1995-07-07 2004-03-08 本田技研工業株式会社 Fuel cell and its fastening method
JP4410965B2 (en) * 2001-10-18 2010-02-10 株式会社荏原製作所 Power generation method using fuel cell power generation system and fuel cell power generation system
US20040028972A1 (en) * 2002-08-12 2004-02-12 General Electric Company Method and apparatus for fuel cell thermal management
JP4992188B2 (en) * 2005-03-11 2012-08-08 株式会社エクォス・リサーチ Separator unit and fuel cell stack
JP5090651B2 (en) * 2006-03-02 2012-12-05 本田技研工業株式会社 Fuel cell
JP5063619B2 (en) * 2009-01-14 2012-10-31 三洋電機株式会社 Fuel cell system

Also Published As

Publication number Publication date
JPH0620713A (en) 1994-01-28

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