JPS6323621B2 - - Google Patents
Info
- Publication number
- JPS6323621B2 JPS6323621B2 JP57157133A JP15713382A JPS6323621B2 JP S6323621 B2 JPS6323621 B2 JP S6323621B2 JP 57157133 A JP57157133 A JP 57157133A JP 15713382 A JP15713382 A JP 15713382A JP S6323621 B2 JPS6323621 B2 JP S6323621B2
- Authority
- JP
- Japan
- Prior art keywords
- air
- reaction
- manifold
- cooling
- cooling plate
- 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
Links
- 238000001816 cooling Methods 0.000 claims description 55
- 239000000446 fuel Substances 0.000 claims description 10
- 238000004891 communication Methods 0.000 claims description 8
- 238000000926 separation method Methods 0.000 description 8
- 239000007789 gas Substances 0.000 description 7
- 239000002737 fuel gas Substances 0.000 description 5
- 239000012495 reaction gas Substances 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000009499 grossing Methods 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 230000036647 reaction Effects 0.000 description 1
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
- H01M8/04007—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
- H01M8/04014—Heat exchange using gaseous fluids; Heat exchange by combustion of reactants
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0267—Collectors; Separators, e.g. bipolar separators; Interconnectors having heating or cooling means, e.g. heaters or coolant flow channels
-
- 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
- H01M8/241—Grouping of fuel cells, e.g. stacking of fuel cells with solid or matrix-supported electrolytes
-
- 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
- H01M8/2457—Grouping of fuel cells, e.g. stacking of fuel cells with both reactants being gaseous or vaporised
-
- 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
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Fuel Cell (AREA)
- Combustion & Propulsion (AREA)
Description
【発明の詳細な説明】
技術分野
本発明は空冷式燃料電池特に冷却空気を反応空
気と分離供給する方式の燃料電池に関するもので
ある。DETAILED DESCRIPTION OF THE INVENTION Technical Field The present invention relates to an air-cooled fuel cell, and particularly to a fuel cell in which cooling air is supplied separately from reaction air.
背景技術
燃料電池の冷却用空気の供給方法は、反応用空
気と共に同一マニホルドに送り、反応空気はガス
分離板の通路へ、冷却空気は冷却板の通路へ夫々
導入する方法と、反応空気とは分離して冷却空気
専用マニホルドへ供給する方法とがある。BACKGROUND TECHNOLOGY There are two methods for supplying cooling air to a fuel cell: sending it together with the reaction air to the same manifold, and introducing the reaction air into the passage of the gas separation plate and the cooling air into the passage of the cooling plate, respectively.What is the reaction air? There is a method of separating the air and supplying it to a dedicated cooling air manifold.
前者は各通路のパターンが簡単であるという利
点があるが、反応空気と冷却空気は分離していな
いので個々に必要とされる空気量を送ることが不
可能であり、電池反応と電池温度とのバランスが
くずれることになり電池特性上好ましくない。 The former has the advantage that the pattern of each passage is simple, but since the reaction air and cooling air are not separated, it is impossible to send the required amount of air individually, and the battery reaction and temperature This is unfavorable from the viewpoint of battery characteristics.
一方後者は第1図、第2図のようなスタツクイ
とマニホルドロを用いて冷却空気と、反応空気を
分離供給するが、冷却空気通路及び反応ガス(空
気及び燃料ガス)通路のパターンが複雑となつて
反応ガス分離板及び冷却板の作成がむつかしいと
共に流通抵抗が大きくなつて大容量のブロワを必
要とするなどの問題点があつた。 On the other hand, in the latter case, cooling air and reaction air are separately supplied using a stacker and a manifold drawer as shown in Figures 1 and 2, but the patterns of cooling air passages and reaction gas (air and fuel gas) passages are complicated. However, there were problems in that it was difficult to fabricate the reaction gas separation plate and the cooling plate, and the flow resistance increased, requiring a large-capacity blower.
発明の開示
本発明は冷却空気と反応空気を共通に供給する
方式のスタツクにわずかの改良を加えることによ
り、冷却空気と反応空気とを分離供給できるよう
にしたもので、その特徴とする所は、電池スタツ
クに介在する各冷却板を、スタツクの少くとも空
気導入面より突設して前記スタツクに取付けた反
応空気用マニホルドの窓口に気密的に装着し、前
記各窓部に冷却板の空気通路を露出させると共に
前記反応空気用マニホルド上に冷却空気用マニホ
ルドを取付けた点にある。DISCLOSURE OF THE INVENTION The present invention makes it possible to separately supply cooling air and reaction air by making slight improvements to the stack that commonly supplies cooling air and reaction air. , each cooling plate interposed in the battery stack is airtightly attached to a window of a reaction air manifold attached to the stack so as to protrude from at least the air introduction surface of the stack, and air from the cooling plate is inserted into each window. The passage is exposed and a cooling air manifold is mounted on the reaction air manifold.
又反応空気用マニホルドの一側面には、各冷却
板間のサブスタツクに対応する連通口を穿設する
と共にこれら連通口を覆う補助マニホルドを取付
けてもよい。 Further, communication ports corresponding to the substack between each cooling plate may be provided on one side of the reaction air manifold, and an auxiliary manifold may be attached to cover these communication ports.
更に冷却板が突設しない空気導出面には、反応
空気及び冷却空気の共通マニホルドを取付けて構
成の簡単化を図ることも可能である。 Furthermore, it is also possible to simplify the configuration by attaching a common manifold for reaction air and cooling air to the air outlet surface where the cooling plate does not protrude.
実施例
本発明の実施例を第3図乃至第5図について説
明する。Embodiment An embodiment of the present invention will be described with reference to FIGS. 3 to 5.
電池スタツク1は周知のように、陰陽ガス極間
に電解質マトリツクスを介挿した単位セル2と、
両面に互に交錯する方向に各反応ガス通路を配列
した炭素質ガス分離板3とを交互に多数積重し、
4〜5単位セル毎に空気通路4を有する炭素質冷
却板5を介在させ、上下端板6,6間で締付けて
構成される。 As is well known, the battery stack 1 includes a unit cell 2 in which an electrolyte matrix is inserted between negative and positive gas electrodes;
A large number of carbonaceous gas separation plates 3 each having reaction gas passages arranged in intersecting directions on both sides are stacked alternately,
A carbonaceous cooling plate 5 having an air passage 4 is interposed between every 4 to 5 unit cells, and the upper and lower end plates 6 are tightened together.
本発明の冷却板5は第4図に示すようにスタツ
ク1の空気流通面より夫々突設し、これら各突設
部5′,5′をスタツク1に取付けた反応空気用の
各マニホルド7の窓口7′に気密的に装着し、各
窓口7′に冷却板5の空気通路4を露出させてい
る。これら空気通路4を覆うように、反応空気用
各マニホルド7,7上に冷却空気用の各マニホル
ド8,8を取付ける。 As shown in FIG. 4, the cooling plates 5 of the present invention are respectively protruded from the air flow surface of the stack 1, and these protrusions 5', 5' are connected to each manifold 7 for reaction air attached to the stack 1. The cooling plate 5 is airtightly attached to the window 7', and the air passage 4 of the cooling plate 5 is exposed to each window 7'. Cooling air manifolds 8, 8 are mounted on the reaction air manifolds 7, 7 so as to cover these air passages 4.
反応空気用の各マニホルド7,7の一側面に
は、各冷却板間のサブスタツク1′に対応して
夫々連通口9を穿設すると共にこれら連通口9を
覆うように補助マニホルド10を取付けている。
尚スタツク1の水素流通面には従来と同様反応水
素用の各マニホルド11,11が取付けられる。 On one side of each manifold 7 for reaction air, a communication port 9 is provided corresponding to the substack 1' between each cooling plate, and an auxiliary manifold 10 is attached to cover the communication port 9. There is.
Incidentally, manifolds 11, 11 for reacting hydrogen are attached to the hydrogen flow surface of the stack 1, as in the conventional case.
冷却空気は冷却空気導入用マニホルド8に導入
されて、反応空気用マニホルド7の各窓口7′に
露出する各冷却板5の空気通路4を通りスタツク
1を冷却して後冷却空気導出用マニホルド8を経
て外部に排出される。この昇温(約180℃)した
排出空気は熱交換器で冷却(約150℃)され再び
前記の如き冷却空気経路を通つて循環する。かく
て送風空気量の調節によりスタツクの温度を電池
作動温度(180〜190℃)に維持する。 The cooling air is introduced into the cooling air introduction manifold 8, passes through the air passages 4 of each cooling plate 5 exposed at each window 7' of the reaction air manifold 7, cools the stack 1, and is then transferred to the cooling air delivery manifold 8. It is then discharged to the outside. This discharged air whose temperature has been raised (approximately 180°C) is cooled (approximately 150°C) by a heat exchanger and circulated again through the cooling air path as described above. In this way, the temperature of the stack is maintained at the battery operating temperature (180-190°C) by adjusting the amount of air blown.
一方反応空気は、補助マニホルド10に導入さ
れ各連通口9を経て、反応空気導入用マニホルド
7に入り、冷却板5間にサブスタツク1′を構成
するガス分離板2の反応空気通路を通り、ついで
前記とは逆に反応空気導出用マニホルド7一連通
口9―補助マニホルド10を経て排出される。こ
の反応空気は、電池反応に必要な150℃程度の温
度で供給する必要があるので、前記の冷却空気の
排出流を一部利用してもよいし、反応空気の排出
流との間で熱交換して予熱供給してもよい。 On the other hand, the reaction air is introduced into the auxiliary manifold 10, passes through each communication port 9, enters the reaction air introduction manifold 7, passes through the reaction air passage of the gas separation plate 2 forming the substack 1' between the cooling plates 5, and then Contrary to the above, the reaction air is discharged through the manifold 7, the continuous port 9, and the auxiliary manifold 10. This reaction air needs to be supplied at a temperature of about 150°C, which is necessary for the battery reaction, so the exhaust flow of the cooling air described above may be partially used, or the reaction air can be heated between it and the exhaust flow of the reaction air. Preheating may be supplied by exchanging.
燃料改質器から供給される反応燃料ガスは、通
常方式と同様燃料ガス導入用マニホルド11を経
てガス分離板2の燃料ガス通路を通り、反応空気
との間で電池反応にあずかる。 The reaction fuel gas supplied from the fuel reformer passes through the fuel gas introduction manifold 11, the fuel gas passage of the gas separation plate 2, and participates in a cell reaction with the reaction air, as in the normal system.
以上の実施例は冷却板5の空気導入側及び導出
側をスタツク1より突設した場合を示したが、第
6図及び第7図の他実施例は、冷却空気の導入側
は前記実施例と同一構成であるが、導出側は冷却
板5を突出させることなく、通常の如く共通のマ
ニホルド12を取付け冷却空気と反応空気はスタ
ツク1の通過後合体して排出させる場合を示す。 Although the above embodiment shows the case where the air inlet side and the outlet side of the cooling plate 5 are provided protruding from the stack 1, in other embodiments shown in FIGS. 6 and 7, the cooling air inlet side However, on the outlet side, a common manifold 12 is installed as usual without protruding the cooling plate 5, and cooling air and reaction air are combined and discharged after passing through the stack 1.
この他実施例では、反応空気と冷却空気は夫々
独立的に導入されて前記実施例と同様に夫々の送
風空気量の調節が可能であり、導出側は同一のマ
ニホルドを通して排気されるのでこの部分の構成
が簡単化される。又冷却空気量は反応空気量に比
し著しく多いため、反応空気の導出側は減圧とな
つて反応空気を引つぱる状態となり、反応空気の
流れが円滑になるという利点がある。 In other embodiments, the reaction air and the cooling air are each introduced independently and the amount of air blown can be adjusted as in the previous embodiment, and the outlet side is exhausted through the same manifold, so this section The configuration of is simplified. In addition, since the amount of cooling air is significantly larger than the amount of reaction air, the pressure on the outlet side of the reaction air is reduced and the reaction air is pulled, which has the advantage of smoothing the flow of the reaction air.
効 果
本発明によれば、電池スタツクの同一面に冷却
空気用及び反応空気用の各通路が開口する通常の
スタツクを利用し、このスタツクに介在する各冷
却板より突設した部分を反応空気用マニホルドの
窓口に気密的に嵌着してこの窓口に露出する冷却
空気通路を覆うよう反応空気用マニホルド上に冷
却空気用マニホルドを取付けることにより、冷却
空気と反応空気を分離供給するものであるから、
従来の分離供給方式に比し各空気通路のパターン
が極めて単純であり且ガス分離板及び冷却板の作
成が簡単化されると共に各空気の流通が円滑化さ
れてブロワの能力も小さくてすむなどの利点があ
る。Effects According to the present invention, a normal stack in which passages for cooling air and reaction air are opened on the same side of the battery stack is used, and a portion protruding from each cooling plate interposed in this stack is used to direct passages for reaction air. Cooling air and reaction air are separately supplied by installing a cooling air manifold on the reaction air manifold so that it airtightly fits into the window of the reaction manifold and covers the cooling air passage exposed through this window. from,
Compared to the conventional separation supply system, the pattern of each air passage is extremely simple, the creation of the gas separation plate and cooling plate is simplified, the circulation of each air is smoother, and the blower capacity can be reduced. There are advantages.
第1図及び第2図はいずれも従来の分離式冷却
空気経路を有する電池の平面図、第3図乃至第5
図は本発明燃料電池を示し、第3図は同上の斜面
面、第4図は電池スタツクの斜面図、第5図は一
部分解斜面図である。又第6図及び第7図は本発
明の他実施例を示し、第6図は一部分解斜面図、
第7図は電池スタツクの斜面図である。
1……電池スタツク、1′……サブスタツク、
2……単位セル、3……ガス分離板、4……冷却
空気通路、5……冷却板、7……反応空気用マニ
ホルド、7′……窓口、8……冷却空気用マニホ
ルド、9……連通口、10……反応空気用補助マ
ニホルド、11……反応燃料ガス用マニホルド、
12……導出側共通マニホルド。
Figures 1 and 2 are top views of batteries with conventional separate cooling air paths, and Figures 3 to 5 are
The figures show the fuel cell of the present invention, FIG. 3 is a sloped view of the same as above, FIG. 4 is a sloped view of a cell stack, and FIG. 5 is a partially exploded sloped view. Further, FIGS. 6 and 7 show other embodiments of the present invention, and FIG. 6 is a partially exploded slope view,
FIG. 7 is a perspective view of the battery stack. 1...Battery stack, 1'...Sub stack,
2... Unit cell, 3... Gas separation plate, 4... Cooling air passage, 5... Cooling plate, 7... Manifold for reaction air, 7'... Window, 8... Manifold for cooling air, 9... ... Communication port, 10 ... Auxiliary manifold for reaction air, 11 ... Manifold for reaction fuel gas,
12... Output side common manifold.
Claims (1)
ツクを備えた空冷式燃料電池において、前記冷却
板は少くとも反応空気導入面に前記冷却通路が開
口した突設部を有しており、更に前記突設部に対
応した位置に窓口が開口されている反応空気用マ
ニホルドと、前記マニホルド上に取付けた冷却空
気用マニホルドとを設け、前記突設部を前記窓口
に気密的に装着したことを特徴とする空冷式燃料
電池。 2 前記反応空気用マニホルドの一側面には、各
冷却板間のサブスタツクに対応して連通口を穿設
すると共にこれら連通口を覆う補助マニホルドを
取付けたことを特徴とする特許請求の範囲第1項
記載の空冷式燃料電池。 3 前記冷却板が反応空気導入面及び導出面に
夫々突設部を有していることを特徴とする特許請
求の範囲第1項もしくは第2項記載の空冷式燃料
電池。 4 前記冷却板が突設しない前記反応空気導出面
には、反応空気及び冷却空気の共通マニホルドを
取付けたことを特徴とする特許請求の範囲第1項
もしくは第2項記載の空冷式燃料電池。[Scope of Claims] 1. In an air-cooled fuel cell equipped with a cell stack including a cooling plate in which a cooling passage is formed, the cooling plate has a protruding portion in which the cooling passage is opened at least on a reaction air introduction surface. Further, a reaction air manifold having a window opened at a position corresponding to the protruding part, and a cooling air manifold mounted on the manifold are provided, and the protruding part is airtightly connected to the window. An air-cooled fuel cell characterized by being installed in. 2. The first aspect of the present invention is characterized in that communication ports are formed on one side of the reaction air manifold corresponding to the sub-stack between each cooling plate, and an auxiliary manifold is attached to cover these communication ports. The air-cooled fuel cell described in Section 1. 3. The air-cooled fuel cell according to claim 1 or 2, wherein the cooling plate has protrusions on the reaction air introduction surface and the reaction air exit surface, respectively. 4. The air-cooled fuel cell according to claim 1 or 2, wherein a common manifold for reaction air and cooling air is attached to the reaction air outlet surface where the cooling plate does not protrude.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57157133A JPS5946769A (en) | 1982-09-08 | 1982-09-08 | Air-cooled fuel cell |
| US06/528,443 US4508793A (en) | 1982-09-08 | 1983-09-01 | Air-cooled fuel cell system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57157133A JPS5946769A (en) | 1982-09-08 | 1982-09-08 | Air-cooled fuel cell |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5946769A JPS5946769A (en) | 1984-03-16 |
| JPS6323621B2 true JPS6323621B2 (en) | 1988-05-17 |
Family
ID=15642920
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57157133A Granted JPS5946769A (en) | 1982-09-08 | 1982-09-08 | Air-cooled fuel cell |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5946769A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH03115819U (en) * | 1990-03-14 | 1991-12-02 |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7135247B2 (en) * | 2003-10-23 | 2006-11-14 | Utc Fuel Cells, Llc | Easily isolated, oversized fuel cell stack cooler plates |
-
1982
- 1982-09-08 JP JP57157133A patent/JPS5946769A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH03115819U (en) * | 1990-03-14 | 1991-12-02 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5946769A (en) | 1984-03-16 |
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