JPS62237671A - Electrolyte retaining structure of fuel cell - Google Patents
Electrolyte retaining structure of fuel cellInfo
- Publication number
- JPS62237671A JPS62237671A JP61079933A JP7993386A JPS62237671A JP S62237671 A JPS62237671 A JP S62237671A JP 61079933 A JP61079933 A JP 61079933A JP 7993386 A JP7993386 A JP 7993386A JP S62237671 A JPS62237671 A JP S62237671A
- Authority
- JP
- Japan
- Prior art keywords
- electrolyte
- reservoir
- plate
- fuel cell
- 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.)
- Pending
Links
- 239000003792 electrolyte Substances 0.000 title claims abstract description 73
- 239000000446 fuel Substances 0.000 title claims abstract description 15
- 230000002093 peripheral effect Effects 0.000 claims description 2
- 230000007797 corrosion Effects 0.000 abstract description 5
- 238000005260 corrosion Methods 0.000 abstract description 5
- 239000012495 reaction gas Substances 0.000 abstract description 5
- 230000003247 decreasing effect Effects 0.000 abstract 1
- 238000010248 power generation Methods 0.000 abstract 1
- 230000001502 supplementing effect Effects 0.000 abstract 1
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 6
- 206010026749 Mania Diseases 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 238000012423 maintenance Methods 0.000 description 3
- 229910052697 platinum Inorganic materials 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 239000012466 permeate Substances 0.000 description 2
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
- 239000010457 zeolite Substances 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
- H01M8/04276—Arrangements for managing the electrolyte stream, e.g. heat exchange
- H01M8/04283—Supply means of electrolyte to or in matrix-fuel cells
-
- 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
- H01M8/244—Grouping of fuel cells, e.g. stacking of fuel cells with solid or matrix-supported electrolytes with matrix-supported molten electrolyte
-
- 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
- H01M8/2483—Details of groupings of fuel cells characterised by internal manifolds
-
- 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
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は燃料電池の電解質保持構造に係り、特に電解質
の補給及び電解質の流出防止対策を図った燃料電池のt
解質保持構造に関する。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to an electrolyte holding structure for a fuel cell, and particularly to a fuel cell t-retaining structure that takes measures to replenish electrolyte and prevent electrolyte outflow.
Regarding solute retention structure.
燃料電池は高温でl/I″動しているため、電解質は溶
融状態にある。このため、燃料電池の内部では。Since the fuel cell operates at high temperature and l/I'', the electrolyte is in a molten state. Therefore, inside the fuel cell.
反応ガスによって′lt解質が外部へ運び去られ、更に
は電池外周部から溶けた電解質が流れ出す等により、多
くのIt電解質消失している。Much of the It electrolyte is lost due to the reactive gas carrying away the It electrolyte to the outside, and the melted electrolyte flowing out from the outer periphery of the battery.
この電解質の消失防止策として、特に電解質補給構造の
面からの提案が従来より種々なされている。例えば、セ
パレータのウェットシール部に電解質を溜めておく溝が
形成され、この溝に予め電解質をr=iめておくものが
ある。この型式では成る決まった清しか’gIt解質を
補給できないため、運転中の補給電が零になった場合、
電池を分解し、再補給する手段がとられる。As a measure to prevent the loss of electrolyte, various proposals have been made in the past, particularly from the perspective of electrolyte replenishment structures. For example, there is a separator in which a groove for storing an electrolyte is formed in the wet seal portion of the separator, and the electrolyte is previously stored in this groove at r=i. In this model, only a fixed amount of 'gIt solute can be supplied, so if the supply power becomes zero during operation,
Measures are taken to disassemble and replenish the battery.
なお、この棟の装置として関連するものには、例えば、
v!ti昭58−23166号が挙げられる。In addition, related equipment in this building includes, for example,
v! Ti No. 58-23166 is mentioned.
しかし、上記従来技術は、運転中に補給量が零になった
場合、電池を分解して補給せねばならないため、メンテ
ナンス性が悪いばかりか、運転状態によっては過剰電解
質となり、外周部より溢れ出る等の問題があった。However, with the above conventional technology, if the replenishment amount becomes zero during operation, the battery must be disassembled and replenished, which not only makes maintenance difficult, but also causes excess electrolyte to overflow from the outer periphery depending on the operating conditions. There were other problems.
本発明の目的は、を解質板の状態に合せて電解質補給、
vL解質流出防止に対しメンテナンスの簡単な燃料電池
の電解質保持構造を提供することに1ある。The purpose of the present invention is to replenish electrolytes according to the state of the electrolyte plate,
One object of the present invention is to provide an electrolyte holding structure for a fuel cell that is easy to maintain and prevents VL electrolyte outflow.
上記目的は、燃料電池の外周面に電解質溜り部を設け、
補給時には前記溜り部に電解質を導入し。The above purpose is to provide an electrolyte reservoir on the outer peripheral surface of the fuel cell,
When replenishing, electrolyte is introduced into the reservoir.
過剰時には電解質が前記溜り部に溢れ出るようにするこ
とにより達成される。This is achieved by allowing the electrolyte to overflow into the reservoir in case of excess.
’1ets質板の外周部に配設した電解質溜め部には、
′電解質の供給及び過剰電解質の受は入れ部として機能
する。これによって、供給した電解質は電解質板側面よ
シ浸透して内部へ含浸し、また過剰電解質は外部Klれ
出ないので、メンテナンスが容易となる。In the electrolyte reservoir located on the outer periphery of the 1ets quality plate,
'The supply of electrolyte and the reception of excess electrolyte function as a receptacle. As a result, the supplied electrolyte permeates through the side surface of the electrolyte plate and impregnates the inside, and excess electrolyte does not leak out to the outside, making maintenance easier.
以下1本発明の一実施例を第1図及び第2図により説明
する。第1図において、・燃料電池は、端板1とセパレ
ータ2間に電極3を配設し、且つ電極3の片側に反応ガ
ス通路4を設けて構成される。An embodiment of the present invention will be described below with reference to FIGS. 1 and 2. In FIG. 1, the fuel cell is constructed by having an electrode 3 disposed between an end plate 1 and a separator 2, and a reaction gas passage 4 provided on one side of the electrode 3.
電極3間には′rii解質板5が設けられ、この1解質
板5と電極3は、故ブロックが積層された構造となって
いる。また、端板lの端部には、グレート構造物6が設
けられ、マニフオールド7を形成シている。A 'rii solute plate 5 is provided between the electrodes 3, and this solute plate 5 and the electrode 3 have a structure in which blocks are laminated. Furthermore, a grate structure 6 is provided at the end of the end plate l, forming a manifold 7.
このような構造の燃料電池にあって、電解質保持構造と
してのゼ解買溜め部8が、セパレータ2の端市部KL字
形所面を有するように設けられている。In a fuel cell having such a structure, a zeolite storage section 8 serving as an electrolyte holding structure is provided so as to have a KL-shaped end portion of the separator 2.
、π2図は第1図の実権例の平面図である。第2図に示
すように−4解質溜め部8は、マニフオールド7をプレ
ート構造物6に凄触するように端部が加工されている。, π2 is a plan view of the actual example shown in FIG. As shown in FIG. 2, the end of the -4 solute reservoir 8 is machined so that the manifold 7 comes into contact with the plate structure 6.
以上の構成において、反応ガスは、マニアオールド7内
に導入されたのち、電解質溜め部8を乗り越えて、ガス
流路4へ供給される。In the above configuration, the reaction gas is introduced into the manifold old 7 and then overcomes the electrolyte reservoir 8 and is supplied to the gas flow path 4.
電解質板5中の電解質が消失し、電池性能の低下が認め
られた場合には1反応ガスの導入を一旦停止し、プレー
ト構造物6を端板1から取外し。When the electrolyte in the electrolyte plate 5 disappears and a decrease in battery performance is observed, the introduction of the reactant gas is temporarily stopped, and the plate structure 6 is removed from the end plate 1.
電解質溜め部8の各々へ、第3図の様に電解質9を導入
してやる。ついでプレート構造物6を端板1に取付けた
のち1反応ガスをマニアオールド7内に導入する。この
とき、マニアオールド7内の圧力P+ をt@質版板5
中圧力Pzよりも高くすることによって、電解質溜め部
8に導入した電解質9は、1解質板5の端面よシ破線矢
印方向に浸透してゆき、心解貞板5にcft屏質9が補
給される。Electrolyte 9 is introduced into each electrolyte reservoir 8 as shown in FIG. Next, after attaching the plate structure 6 to the end plate 1, one reaction gas is introduced into the mania old 7. At this time, the pressure P+ in the mania old 7 is changed to t@quality plate 5
By setting the pressure higher than the medium pressure Pz, the electrolyte 9 introduced into the electrolyte reservoir 8 permeates from the end face of the electrolyte plate 5 in the direction of the broken line arrow, and the CFT platinum 9 is deposited on the heart release plate 5. will be replenished.
このとき、マニアオールド7内の圧力P+t’4解質板
5の許容耐圧以上に高くすることは好ましく無い。At this time, it is not preferable to make the pressure inside the mania old 7 higher than the allowable withstand pressure of the decomposition plate 5 (P+t'4).
また、起動時及び発成中断時にあって反応ガスの導入が
停止された場合、1!屏質の消費が無いため、溶融した
IE屏質が端板lよシ直接に流出してくる。この電解質
は、電解質溜め部8に溜fす。In addition, if the introduction of the reaction gas is stopped during startup or generation interruption, 1! Since there is no consumption of platinum, the molten IE platinum directly flows out from the end plate l. This electrolyte is stored in the electrolyte reservoir 8.
外部への流出が防止される。この結果、セパレータ2の
端面の電解質による腐食が防止される。External leakage is prevented. As a result, corrosion of the end face of the separator 2 due to the electrolyte is prevented.
第4図は電解質溜め部の他の例を示し、L字形断面を有
する溜め部材10をセパレータ2の端部へ溶接等によっ
て固定することにより、電解質溜め部8を形成するよう
にしたものである。溜め部材IOは、耐食性の高い材質
、例えばセラミックス等を用いることができる。第4図
の如き構成にすることによって部品数が増えるが、構造
が単純化するため、加工性を上げ、更には電解質溜め部
8の腐食を防止することができる。FIG. 4 shows another example of the electrolyte reservoir, in which an electrolyte reservoir 8 is formed by fixing a reservoir member 10 having an L-shaped cross section to the end of the separator 2 by welding or the like. . The reservoir member IO can be made of a material with high corrosion resistance, such as ceramics. Although the configuration shown in FIG. 4 increases the number of parts, it simplifies the structure, improves workability, and furthermore prevents corrosion of the electrolyte reservoir 8.
尚、腐食生成物が混入していない流出電解質は。In addition, the effluent electrolyte is free from corrosion products.
再度補給することも可能である。It is also possible to replenish.
〔発明の効果〕
以上説明した通り1本発明によれば、電解質の補給及び
流出防止に対するメンテナンスが簡単な構成によって実
現でさるため、It屏質板を長期的に安定な性能を維持
することができ1電池の長寿命化を図ることができる。[Effects of the Invention] As explained above, according to the present invention, maintenance for electrolyte replenishment and outflow prevention can be achieved with a simple configuration, making it possible to maintain stable performance of the IT board over a long period of time. Therefore, it is possible to extend the life of one battery.
第1図は本発明の一実施例を示す燃料電池を示す側面断
面図、第2図は第1図の実施例の平面図。
第3図は本発明の実施例の動作説明図、第4図は電解質
溜め部の他の実施例を示す断面図である。
■・・・端板、2・・・セパレータ、3・・・電極、4
・・・通路。
5・・・電解質板、6・・・プレート構造物、7・・・
マニフオールド、8・・・電解質溜め部、9・・・電解
質、10・・・溜め部材。
。FIG. 1 is a side sectional view showing a fuel cell showing one embodiment of the present invention, and FIG. 2 is a plan view of the embodiment of FIG. 1. FIG. 3 is an explanatory diagram of the operation of the embodiment of the present invention, and FIG. 4 is a sectional view showing another embodiment of the electrolyte reservoir. ■... End plate, 2... Separator, 3... Electrode, 4
···aisle. 5... Electrolyte plate, 6... Plate structure, 7...
Manifold, 8... Electrolyte reservoir, 9... Electrolyte, 10... Reservoir member.
.
Claims (1)
て配設される電極、該電極間に配設される電解質板の各
々を備えて構成される燃料電池において、前記電解質板
の端部に隣接して電解質溜め部を設けたことを特徴とす
る燃料電池の電解質保持構造。 2、前記電解質溜め部を前記セパレータの外周部に該セ
パレータと一体に形成したことを特徴とする特許請求の
範囲第1項に記載の燃料電池の電解質保持構造。 3、L字形の断面形状を有する溜め部材を前記セパレー
タの外周部に装着して、前記電解質溜め部を構成するこ
とを特徴とする特許請求の範囲第1項に記載の燃料電池
の電解質保持構造。[Scope of Claims] 1. A fuel cell configured to include a separator having a gas flow path, an electrode disposed in contact with the gas flow path, and an electrolyte plate disposed between the electrodes, An electrolyte holding structure for a fuel cell, characterized in that an electrolyte reservoir is provided adjacent to an end of the electrolyte plate. 2. The electrolyte holding structure for a fuel cell according to claim 1, wherein the electrolyte reservoir is formed integrally with the separator at an outer peripheral portion of the separator. 3. The electrolyte holding structure for a fuel cell according to claim 1, wherein a reservoir member having an L-shaped cross section is attached to the outer periphery of the separator to constitute the electrolyte reservoir. .
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61079933A JPS62237671A (en) | 1986-04-09 | 1986-04-09 | Electrolyte retaining structure of fuel cell |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61079933A JPS62237671A (en) | 1986-04-09 | 1986-04-09 | Electrolyte retaining structure of fuel cell |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS62237671A true JPS62237671A (en) | 1987-10-17 |
Family
ID=13704115
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61079933A Pending JPS62237671A (en) | 1986-04-09 | 1986-04-09 | Electrolyte retaining structure of fuel cell |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62237671A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2000059060A1 (en) * | 1999-03-29 | 2000-10-05 | Siemens Aktiengesellschaft | Htm fuel cell or battery with reduced washing-out of the electrolyte, and starting method |
US11444298B2 (en) | 2019-07-18 | 2022-09-13 | Hyaxiom, Inc. | Electrolyte shunt migration management in a fuel cell stack |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5983357A (en) * | 1982-09-30 | 1984-05-14 | エンゲルハ−ド・コ−ポレ−シヨン | System for supplying electrolyte to fuel battery |
JPS60225365A (en) * | 1984-04-23 | 1985-11-09 | Fuji Electric Corp Res & Dev Ltd | Electrolyte supplementing structure for matrix type fuel cell |
JPS6298568A (en) * | 1985-10-25 | 1987-05-08 | Fuji Electric Co Ltd | Cell structure of molten carbonate type fuel cell |
-
1986
- 1986-04-09 JP JP61079933A patent/JPS62237671A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5983357A (en) * | 1982-09-30 | 1984-05-14 | エンゲルハ−ド・コ−ポレ−シヨン | System for supplying electrolyte to fuel battery |
JPS60225365A (en) * | 1984-04-23 | 1985-11-09 | Fuji Electric Corp Res & Dev Ltd | Electrolyte supplementing structure for matrix type fuel cell |
JPS6298568A (en) * | 1985-10-25 | 1987-05-08 | Fuji Electric Co Ltd | Cell structure of molten carbonate type fuel cell |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2000059060A1 (en) * | 1999-03-29 | 2000-10-05 | Siemens Aktiengesellschaft | Htm fuel cell or battery with reduced washing-out of the electrolyte, and starting method |
US11444298B2 (en) | 2019-07-18 | 2022-09-13 | Hyaxiom, Inc. | Electrolyte shunt migration management in a fuel cell stack |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP5265080B2 (en) | Bipolar plate for fuel cell | |
JPH06275285A (en) | Fuel cell, electrolyte supply container, and electrolyte supplying method | |
JPS62237671A (en) | Electrolyte retaining structure of fuel cell | |
JP2007157351A (en) | Fuel cell stack and fuel cell | |
JPS61277169A (en) | Cell structure of molten carbonate type fuel cell | |
CA2410005C (en) | Fuel cell assembly comprising an electrolyte reservoir | |
JPH0145095Y2 (en) | ||
JPH05343079A (en) | Gas seal structure for solid electrolyte fuel cell | |
US4702972A (en) | Electrolyte replenishing system for a laminated fuel cell | |
JP2005050699A (en) | Lead-acid storage battery | |
JP3066461B2 (en) | Fuel cell separator | |
JPH01195669A (en) | Fused carbonate type fuel cell and electrolyte supplying method to it | |
JPS6298568A (en) | Cell structure of molten carbonate type fuel cell | |
JPS63175353A (en) | Phosphric fuel cell | |
CN217035691U (en) | Integrated cooling liquid kettle and cooling system | |
JPS61269861A (en) | Cell structure of molten carbonate fuel cell | |
JPH03291856A (en) | Fuel cell | |
JPH08321318A (en) | Electrolyte refilling device of fused carbonate type fuel cell | |
JP2003007286A (en) | Water replenishing faucet for lead-acid battery | |
JPH01279571A (en) | Molten carbonate fuel cell | |
JPS62234870A (en) | Fused carbonate fuel cell | |
JPS6362158A (en) | Device for replenishing electric solution for fuel cell | |
JPH077671B2 (en) | Fuel cell | |
JPH0754708B2 (en) | Molten carbonate fuel cell | |
JPH01235163A (en) | Alkaline fuel cell |