JPH0652667B2 - Fuel cell - Google Patents
Fuel cellInfo
- Publication number
- JPH0652667B2 JPH0652667B2 JP62240751A JP24075187A JPH0652667B2 JP H0652667 B2 JPH0652667 B2 JP H0652667B2 JP 62240751 A JP62240751 A JP 62240751A JP 24075187 A JP24075187 A JP 24075187A JP H0652667 B2 JPH0652667 B2 JP H0652667B2
- Authority
- JP
- Japan
- Prior art keywords
- electrolyte
- reaction gas
- matrix substrate
- fuel cell
- battery
- 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 - Fee Related
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
- H01M8/04276—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
- H01M8/2418—Grouping by arranging unit cells in a plane
-
- 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
-
- 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)
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補給に係り、特に積層型燃料
電池における電解質の外部からの補給機能を備えた燃料
電池に関する。Description: TECHNICAL FIELD The present invention relates to replenishment of an electrolyte for a fuel cell, and more particularly to a fuel cell having a function of replenishing the electrolyte from the outside in a stacked fuel cell.
燃料電池では、電解質板の両側に一対の電極が配設され
それぞれの電極の外側には酸化剤ガス,燃料ガスの流通
路を備えたセパレータが配置されて単位電池を構成して
いる。In a fuel cell, a pair of electrodes are arranged on both sides of an electrolyte plate, and a separator having a passage for an oxidant gas and a fuel gas is arranged outside each electrode to form a unit cell.
電力用燃料電池として大容量化を図るには電極面積を大
きくし、かつ単位電池を多数積層した大形積層電池が標
準スタックとなり、これを複数個集積することにより、
ニーズに見合った規模の発電プラントが構築されること
になる。燃料電池の運転において最も大きな問題点の一
つとして、電解質の単位電池内部あるいは積層電池全体
としての電解質の移動,セパレータ等の腐食による電解
質の損耗や電解質自身の蒸発,飛散による電池外部への
散逸によって電解質が不足し、電池性能が徐々に低下す
るという問題がある。このような問題点に対応する方法
として、これまでにも電池内部に電解質を貯蔵する方法
や外部から電解質を補給する方法が種々提案されてい
る。In order to increase the capacity as a fuel cell for electric power, the electrode area is increased, and a large stacked battery in which a large number of unit batteries are stacked becomes a standard stack.
A power plant of a scale that meets the needs will be built. One of the biggest problems in the operation of fuel cells is the movement of the electrolyte inside the unit cell or the entire laminated cell, the electrolyte wear due to the corrosion of the separator, etc., and the electrolyte itself evaporating and scattering to the outside of the cell. Therefore, there is a problem that the electrolyte becomes insufficient and the battery performance gradually deteriorates. As methods for coping with such problems, various methods have been proposed so far for storing an electrolyte inside a battery and replenishing the electrolyte from the outside.
電解質を電池内部に貯蔵する方法に関連する発明として
は、例えば特開昭53−30747号,特開昭56−54770号,特
開昭58−100368号,特開昭58−138268号,特開昭58−16
5258号,特開昭58−165262号,特開昭58−166653号など
が開示されている。Examples of the invention relating to the method of storing the electrolyte inside the battery include, for example, JP-A-53-30747, JP-A-56-54770, JP-A-58-100368, and JP-A-58-138268. 58-16
5258, JP-A-58-165262 and JP-A-58-166653 are disclosed.
しかし、燃料電池本体に要求されている耐久時間は一般
に約4万時間と言われており、長期にわたって安定な電
池性能を維持する必要があり、電解質の電池内部貯蔵方
式ではなかなかその目標を達成するのは困難である。し
たがって、電池性能が任意の所定値まで低下した時点
で、外部から電解質を電池内部に補給する必要性がでて
くる。However, the durability time required for the fuel cell body is generally said to be about 40,000 hours, and it is necessary to maintain stable cell performance for a long period of time, and it is quite possible to achieve that goal with the electrolyte battery internal storage method. Is difficult. Therefore, when the battery performance drops to an arbitrary predetermined value, it becomes necessary to replenish the inside of the battery with the electrolyte from the outside.
電解質を外部から補給する方法に関連する発明として
は、特開昭57−197756号,特開昭58−42179号,特開昭5
8−61574号,特開昭58−61575号,特開昭58−144760号
などが開示されているが、次のような問題点がある。Inventions relating to a method of replenishing an electrolyte from the outside are disclosed in JP-A-57-197756, JP-A-58-42179, and JP-A-5-42179.
8-61574, JP-A-58-61575 and JP-A-58-144760 are disclosed, but they have the following problems.
これらの発明のいずれにおいても、積層型燃料電池の上
部から下部に貫通する電解質補給口に電解質を充填補給
し、その電解質補給貫通口から分岐して連通する通路を
経て各単位電池に電解質マトリクス基板細孔内に電解質
を補給するものであり、そのための種々の発明が開示さ
れている。しかしながら、上記従来技術においては、上
部から下部への貫通口へ電解質を充填補給するため積層
型燃料電池内での液短絡が起る。In any of these inventions, an electrolyte replenishing port penetrating from the upper part to the lower part of the stacked fuel cell is filled with electrolyte and replenished with electrolyte, and an electrolyte matrix substrate is provided for each unit cell via a passage branched and communicating from the electrolyte replenishing through port. An electrolyte is supplied to the inside of the pores, and various inventions for that purpose are disclosed. However, in the above-mentioned conventional technique, a liquid short circuit occurs in the stacked fuel cell because the electrolyte is filled and replenished to the through holes from the upper part to the lower part.
すなわち、従来は1本若しくは比較的少ない複数の電解
質供給管から電解質が供給されるため、かなり長時間
(数時間〜数十時間)を要して電解質がマトリクス基板
細孔内に浸透するのでセル間で液がつながり易かった。
また、積層型燃料電池の上部単位電池と下部単位電池と
では、ヘッド差の影響もあり、均等に所望の量の電解質
が補給されにくい。That is, conventionally, since the electrolyte is supplied from one or a plurality of relatively few electrolyte supply pipes, it takes a considerably long time (several hours to several tens of hours) and the electrolyte permeates into the matrix substrate pores. The liquid was easy to connect between.
Further, in the upper unit cell and the lower unit cell of the stacked fuel cell, there is an influence of the head difference, and it is difficult to uniformly supply a desired amount of electrolyte.
望ましくは、各単位電池の電池性能の発電の程度に応じ
て、必要量の電解質を別個に各単位電池に補給できるの
がよい。Desirably, a required amount of electrolyte may be separately replenished to each unit battery according to the degree of power generation of the battery performance of each unit battery.
積層型燃料電池の側面部より、各単位電池の電解質マト
リクス基板層へ電解質を注入,補給する方法も考案され
ており、例えば特開昭57−55071号,特開昭58−158870
号,特開昭58−161267号などが開示されている。A method of injecting and replenishing the electrolyte from the side surface of the laminated fuel cell to the electrolyte matrix substrate layer of each unit cell has also been devised, for example, JP-A-57-55071 and JP-A-58-158870.
Japanese Patent Laid-Open No. 58-161267 and the like are disclosed.
しかし、なるべく単位電池当たりの厚さを薄くするのが
望ましいという点から考えると、積層型燃料電池の側面
部から電解質を補給する方式はスペース的な制約を受け
るし、外部マニホールド方式の積層型燃料電池において
は実用化が困難である。However, considering that it is desirable to reduce the thickness per unit cell as much as possible, the method of replenishing the electrolyte from the side surface of the laminated fuel cell is limited in space and the external manifold type laminated fuel is used. Practical application is difficult in batteries.
本発明の目的は、電解質が不足して電池性能が低下する
のを防ぐため、電解質を各単位電池の電解質マトリクス
基板に均質に、しかもスムーズに補給し、長期にわたり
安定した電池性能が得られるようにした電解質補給機能
を有する燃料電池を提供することにある。An object of the present invention is to uniformly and smoothly replenish the electrolyte matrix substrate of each unit battery with electrolyte in order to prevent deterioration of battery performance due to lack of electrolyte, so that stable battery performance can be obtained for a long period of time. Another object of the present invention is to provide a fuel cell having an electrolyte replenishing function.
上記問題点は、電解質マトリクス基板を該電解質マトリ
クス基板より小面積の一対の電極で挟持してなる単位電
池を前記電解質マトリクス基板と略同面積のセパレータ
を介して複数積層した積層体と、前記積層体の上部に設
けられ各単位電池に反応ガスを給排する上部ガスヘッダ
とを備えるブロック電池を含み、前記セパレータは前記
各電極に面して反応ガス流通路を備えると共に前記各電
極の周囲に前記電解質マトリクス基板と接するウエット
シール部を有する燃料電池において、外部から電解質が
供給される電解質分配容器と、該電解質分配容器に連通
する複数の電解質溜と、前記各電解質溜と前記各電解質
マトリクス基板とを連通する前記電解質マトリクス基板
と同数の電解質導入管とを備え、前記上部ガスヘッダは
前記電極を挟んで対向するウエットシール部の上方部分
に反応ガス供給部及び反応ガス排出部を有すると共に該
反応ガス供給部及び反応ガス排出部の中間部分に反応ガ
スが流通しない領域を有し、前記電解質分配容器及び電
解質溜は前記上部ガスヘッダの反応ガスが流通しない領
域に配置され、前記電解質導入管は前記ウエットシール
部を貫通し該ウエットシール部において個別の電解質マ
トリクス基板を終端として配置されていることを特徴と
する燃料電池によって解決される。The above-mentioned problem is that a unit battery in which an electrolyte matrix substrate is sandwiched by a pair of electrodes having a smaller area than the electrolyte matrix substrate is laminated with a separator having substantially the same area as the electrolyte matrix substrate interposed therebetween, and the laminate. A block battery having an upper gas header provided on the upper part of the body and supplying / discharging reaction gas to / from each unit battery, wherein the separator is provided with a reaction gas flow passage facing the electrodes and is provided around the electrodes. In a fuel cell having a wet seal part in contact with an electrolyte matrix substrate, an electrolyte distribution container to which an electrolyte is supplied from the outside, a plurality of electrolyte reservoirs communicating with the electrolyte distribution container, the electrolyte reservoirs and the electrolyte matrix substrates. And the same number of electrolyte introducing tubes as the electrolyte matrix substrate communicating with each other, and the upper gas header sandwiches the electrodes. The reaction gas supply part and the reaction gas discharge part are provided in the upper part of the facing wet seal part, and the reaction gas supply part and the reaction gas discharge part have a region where the reaction gas does not flow in the intermediate part, and the electrolyte distribution container and The electrolyte reservoir is arranged in a region where the reaction gas of the upper gas header does not flow, and the electrolyte introduction pipe penetrates through the wet seal portion and is arranged in the wet seal portion by terminating the individual electrolyte matrix substrate. Solved by a fuel cell that does.
前記問題点は、また、電解質マトリクス基板を該電解質
マトリクス基板より小面積の一対の電極で挟持してなる
単位電池を前記電解質マトリクス基板と略同面積のセパ
レータを介して複数積層した積層体と、前記積層体の上
部に設けられ各単位電池に反応ガスを給排する上部ガス
ヘッダとを備えるブロック電池を含み、前記セパレータ
は前記各電極に面して反応ガス流通路を備えると共に前
記各電極の周囲に前記電解質マトリクス基板と接するウ
エットシール部を有する燃料電池において、電解質供給
手段と、該電解質供給手段から電解質が供給される電解
質分配容器と、該電解質分配容器に連通する複数の電解
質溜と、前記各電解質溜と前記各電解質マトリクス基板
とを連通する前記電解質マトリクス基板と同数の電解質
導入管と、前記ブロック電池の発電性能を検知するブロ
ック電池性能検知手段と、前記ブロック電池性能検知手
段の検知信号により前記電解質供給手段に電解質供給指
令を出力する電解質供給指令手段とを備え、前記上部ガ
スヘッダは前記電極を挟んで対向するウエットシール部
の上方部分に反応ガス供給部及び反応ガス排出部を有す
ると共に該反応ガス供給部及び反応ガス排出部の中間部
分に反応ガスが流通ないし領域を有し、前記電解質分配
容器及び電解質溜は前記上部ガスヘッダの反応ガスが流
通しない領域に配置され、前記電解質導入管は前記ウエ
ットシール部を貫通し該ウエットシール部において個別
の電解質マトリクス基板を終端として配置されているこ
とを特徴とする燃料電池によって解決される。The above-mentioned problem is also a laminated body in which a plurality of unit batteries formed by sandwiching an electrolyte matrix substrate with a pair of electrodes having a smaller area than the electrolyte matrix substrate are laminated with a separator having substantially the same area as the electrolyte matrix substrate interposed therebetween. A block battery having an upper gas header provided at an upper portion of the stack and supplying / discharging a reaction gas to / from each unit cell, wherein the separator has a reaction gas flow passage facing the electrodes and a periphery of the electrodes. In a fuel cell having a wet seal part in contact with the electrolyte matrix substrate, an electrolyte supply means, an electrolyte distribution container to which an electrolyte is supplied from the electrolyte supply means, a plurality of electrolyte reservoirs communicating with the electrolyte distribution container, and An electrolyte introduction tube in the same number as the electrolyte matrix substrate, which communicates each electrolyte reservoir with each electrolyte matrix substrate; Block battery performance detection means for detecting the power generation performance of the battery, and an electrolyte supply command means for outputting an electrolyte supply command to the electrolyte supply means by the detection signal of the block battery performance detection means, the upper gas header is the The reaction gas supply part and the reaction gas discharge part are provided in the upper part of the wet seal part facing each other across the electrode, and the reaction gas has a flow or region in the intermediate part of the reaction gas supply part and the reaction gas discharge part. The electrolyte distribution container and the electrolyte reservoir are arranged in a region where the reaction gas of the upper gas header does not flow, and the electrolyte introduction pipe penetrates through the wet seal portion and is arranged in the wet seal portion with an individual electrolyte matrix substrate as a termination. It is solved by a fuel cell characterized by the above.
ブロック電池の上部ガスヘッダは、中央部に反応ガスが
流通しない部分を有し、その部分に電解質分配容器及び
それに連通し個々の単位電池に対応する複数の電解質溜
がコンパクトに収容される。電解質は、ウエットシール
部を貫通する個別の電解質導入管によって複数の電解質
溜から各単位電池の電解質マトリクス基板に高温を保っ
たまま独立して供給される。各電解質マトリクス基板へ
の電解質の補給は、ウエットシール部で行われる。The upper gas header of the block battery has a portion in which a reaction gas does not flow in the central portion, and in the portion, an electrolyte distribution container and a plurality of electrolyte reservoirs communicating with it and corresponding to individual unit cells are compactly housed. The electrolyte is independently supplied from a plurality of electrolyte reservoirs to the electrolyte matrix substrate of each unit cell while maintaining a high temperature by means of individual electrolyte introduction tubes penetrating the wet seal portion. The electrolyte is replenished to each electrolyte matrix substrate at the wet seal portion.
また、電池性能検知手段によって電池の発電性能を監視
し、電解質補給時期を検知することにより、必要なとき
に電解質を自動的に供給することができる。Further, the battery performance detecting means monitors the power generation performance of the battery and detects the electrolyte replenishment time, so that the electrolyte can be automatically supplied when necessary.
以下、本発明による実施例を第1図〜第6図を用いて説
明する。An embodiment according to the present invention will be described below with reference to FIGS.
実施例1 第1図は燃料極1−1と酸化剤極2−1よりなる一対の
電極の間に電解質を保持してなる電解質マトリクス基板
3−1を配設し、それぞれの電極の外側に燃料ガス及び
酸化剤ガスの流通路を備えたセパレータ4−1が配置さ
れる単位電池をn個積層してなる積層型燃料電池5にお
いて、電解質外部補給構造を示す1つの実施例である。
ここで、n個積層型燃料電池5の上端板6、同じく下端
板7、同じく上部ガスヘッダ8、同じく下部ガスヘッダ
9はシール材10及び11を介して一体化されている。
ガスヘッダ8及び9は第1図のA−A′断面を示す第2
図からわかるように、それぞれ燃料ガス供給部12,燃
料ガス排出部13,酸化剤ガス供給部14及び酸化剤ガ
ス排出部15を有しており、燃料ガスは第1図に示す燃
料ガス供給管16より燃料ガス供給部12から各単位電
池の燃料極1−1〜1−n側を流通後、燃料ガス排出部
13を経て燃料ガス排出管17より排出される。第1図
において、酸化剤ガスの供給及び排出管は省略してある
が、燃料ガスと同様、酸化剤ガスは各単位電池の酸化剤
極2−1〜2−n側を流通後排出される。Example 1 FIG. 1 shows an electrolyte matrix substrate 3-1 which holds an electrolyte between a pair of electrodes composed of a fuel electrode 1-1 and an oxidizer electrode 2-1 and is provided outside each electrode. 1 is an example showing an electrolyte external replenishment structure in a stacked fuel cell 5 in which n unit cells in which a separator 4-1 having fuel gas and oxidant gas flow passages is arranged are stacked.
Here, the upper end plate 6, the lower end plate 7, the upper gas header 8, and the lower gas header 9 of the n-piece stacked fuel cell 5 are integrated with each other through the sealing materials 10 and 11.
The gas headers 8 and 9 are the second ones shown in the section AA 'in FIG.
As can be seen from the figure, each has a fuel gas supply unit 12, a fuel gas discharge unit 13, an oxidant gas supply unit 14, and an oxidant gas discharge unit 15, and the fuel gas is the fuel gas supply pipe shown in FIG. After passing through the fuel gas supply unit 12 from the fuel gas supply unit 12 to the fuel electrodes 1-1 to 1-n side of each unit cell, the fuel gas is discharged from the fuel gas discharge pipe 17 through the fuel gas discharge unit 13. In FIG. 1, the supply and discharge pipes of the oxidant gas are omitted, but like the fuel gas, the oxidant gas is discharged after flowing through the oxidant electrodes 2-1 to 2-n side of each unit cell. .
第1図及び第2図の実施例では、該積層燃料電池5の上
部に配設されている上部ガスヘッダ8内の反応ガスが流
通しない中空部に電解質補給機構を有している。すなわ
ち、電解質分配容器18がその中央部に位置しており、
電解質が積層型燃料電池5本体の外部より電解質供給管
19より電解質分配容器18に供給される。供給された
電解質は各単位電池に連通する電解液溜20に、該電解
質分配容器18の周辺部に設けられた狭いチャンネル通
路21を通過して均等に分配される。均等に分配された
電解質は該電解質溜20にそれぞれ設けられた連通孔2
2を経て水平方向に誘導されてなる電解質補給通路23
を通り、そこから該積層型燃料電池5の上下方向に貫通
する各単位電池の電解質マトリクス基板3−1〜3−n
部をそれぞれ終端とするそれぞれ独立した電解質導入管
24−1〜24−nを流下して各単位電池の電解質マト
リクス基板部3に到達し、その細孔内に均等に浸透,含
浸される。電解質分配容器18の設置位置は特に限定さ
れるものではないが、第1図に示すごとく、ガスヘッダ
8,9内の反応ガスが流通しない中空部に設けるのが好
適である。In the embodiment shown in FIGS. 1 and 2, an electrolyte replenishing mechanism is provided in a hollow portion in the upper gas header 8 disposed above the laminated fuel cell 5 in which a reaction gas does not flow. That is, the electrolyte distribution container 18 is located in the central portion,
The electrolyte is supplied to the electrolyte distribution container 18 from the outside of the main body of the stacked fuel cell 5 through the electrolyte supply pipe 19. The supplied electrolyte is evenly distributed to the electrolyte reservoir 20 communicating with each unit cell, passing through a narrow channel passage 21 provided in the periphery of the electrolyte distribution container 18. The evenly distributed electrolyte is provided with a communication hole 2 provided in each electrolyte reservoir 20.
Electrolyte replenishment passage 23 which is guided in the horizontal direction via 2
Electrolyte matrix substrates 3-1 to 3-n of the unit cells that pass through the laminated fuel cell 5 in the vertical direction.
Each of the unit cells terminates in an independent electrolyte introduction tube 24-1 to 24-n, reaches the electrolyte matrix substrate section 3 of each unit battery, and is uniformly permeated and impregnated into the pores. The installation position of the electrolyte distribution container 18 is not particularly limited, but as shown in FIG. 1, it is preferable to provide the electrolyte distribution container 18 in a hollow portion in the gas headers 8 and 9 where the reaction gas does not flow.
上記電解質溜20から水平方向に誘導された該電解質補
給通路23は、前記ガスヘッダ内部に設けてそこから連
通孔22を介して前記上下方向に貫通する電解質導入管
24に連通することもできるし、また前記電解液溜20
から連通孔22を介して前記ガスヘッダ8底部若しくは
ガスヘッダ8の直下部にあるセパレータ4上部に設けて
そこから該電解質導入管24に連通してもよい。The electrolyte replenishing passage 23, which is guided in the horizontal direction from the electrolyte reservoir 20, may be provided inside the gas header and communicate with the electrolyte introducing pipe 24 penetrating in the vertical direction through the communicating hole 22. In addition, the electrolyte reservoir 20
May be provided at the bottom of the gas header 8 or at the upper part of the separator 4 immediately below the gas header 8 through the communication hole 22 and communicated with the electrolyte introduction pipe 24 from there.
該電解質導入管24は電池のガスシール部位に貫通して
設けるのが通常であり、ウエットシールの場合には、各
単位電池の電解質マトリクス基板3を終端とするところ
までのセパレータ4及びマトリクス電解質基板3に貫通
口を設けて連通させることにより該電解質導入管24が
形成される。The electrolyte introduction tube 24 is usually provided so as to penetrate the gas seal portion of the battery. In the case of a wet seal, the separator 4 and the matrix electrolyte substrate up to the point where the electrolyte matrix substrate 3 of each unit battery is terminated. The electrolyte introduction tube 24 is formed by providing a through hole in 3 and communicating them.
この電解質導入管24は上記のごとく、積層型燃料電池
周辺シール部位に貫通して設けるのが通常であるが、第
6図に示すごとく、電池の大面積化を可能とする同一セ
パレータ面内に複数個の単位電池を形成してなる電池の
場合においては、積層電池周辺シール部位のみならず中
央部シール部位にも電解質導入管24を形成してもよ
い。As described above, the electrolyte introduction tube 24 is usually provided so as to penetrate the laminated fuel cell peripheral sealing portion, but as shown in FIG. 6, the electrolyte introduction tube 24 is provided in the same separator surface that enables the area of the cell to be increased. In the case of a battery in which a plurality of unit batteries are formed, the electrolyte introduction tube 24 may be formed not only in the laminated battery peripheral sealing portion but also in the central sealing portion.
これまで、各単位電池への電解質補給は電解質溜20よ
り電解質補給通路23を経て電解質導入管24を通して
実施されると述べたが、その通路は必ずしも1本でなく
てもよく、電池が大面積化すれば、その通路は各単位電
池に対して複数の通路を形成することも可能である。Up to now, it has been stated that the electrolyte replenishment to each unit battery is carried out from the electrolyte reservoir 20 through the electrolyte replenishment passage 23 and the electrolyte introduction pipe 24, but the passage does not necessarily have to be one, and the battery has a large area. If so, it is possible to form a plurality of passages for each unit cell.
本実施例は液体電解質を用いる各種燃料電池、例えばリ
ン酸型,溶融塩型燃料電池などに適用できることは当然
である。Naturally, this embodiment can be applied to various fuel cells using a liquid electrolyte, such as phosphoric acid type and molten salt type fuel cells.
本実施例の方法によれば、電解質の外部からの各単位電
池への均等補給が可能であり、また液短絡も防止でき
る。もちろん、電池運転状態でも実施できる。According to the method of the present embodiment, it is possible to uniformly replenish the electrolyte from the outside to each unit cell, and it is possible to prevent a liquid short circuit. Of course, it can be carried out even when the battery is operating.
実施例2 第5図は約20〜25セル積層電池を1ブロックとし、
中間に設置したガスヘッダ9を介して2ブロック積層し
た多ブロック積層電池スタックの概略図である。このケ
ースにおいても、上部ブロックへの電解質補給は最上部
のガスヘッダ8より、また下部ブロックへの電解質補給
は中間のガスヘッダ9から、前述の実施例1と同様の方
法により行うことが可能である。この実施例においては
ブロック単位で電解質の補給を制御実行できる。Example 2 In FIG. 5, about 20 to 25 cell laminated battery is regarded as one block,
It is a schematic diagram of a multi-block laminated battery stack in which two blocks are laminated with a gas header 9 installed in the middle. Also in this case, it is possible to replenish the upper block with the electrolyte from the uppermost gas header 8 and replenish the lower block with the intermediate gas header 9 in the same manner as in the first embodiment. In this embodiment, the electrolyte replenishment can be controlled and executed in block units.
このように数セルないし数十セルの積層型燃料電池を1
ブロックとし、中間ガスヘッダを介してこれを複数ブロ
ック積層してなる大容量スタックの場合においても、各
ブロックの上部ガスヘッダ8の中空部に該電解質分配容
器18を設置することができ、各ブロック毎に、あるい
は全ブロックに電解質を供給することも可能である。In this way, a stacked fuel cell with several cells or several tens of cells
Even in the case of a large-capacity stack formed by stacking a plurality of blocks through intermediate gas headers, the electrolyte distribution container 18 can be installed in the hollow portion of the upper gas header 8 of each block, and each block can be installed. Alternatively, it is possible to supply the electrolyte to all blocks.
実施例3 電解質の供給装置と供給手順を第3図及び第4図を用い
て記述する。Example 3 The electrolyte supplying device and the supplying procedure will be described with reference to FIGS. 3 and 4.
第3図は前述したブロック電池単位でその性能を検知し
て性能が予め定めた値より低下したときにブロック電池
毎に電解質を供給する内容を示したものである。FIG. 3 shows the contents of the above-mentioned block batteries which are detected and the electrolyte is supplied to each block battery when the performance is lower than a predetermined value.
第4図は単位電池単位でその性能を検知し、必要に応じ
て電解質を供給する場合の実施例である。以下第3図を
用いて本実施例の内容を記述する。電解質の供給は、電
解質の不足を検知できる各種信号の大小に基づき、その
信号の設定値に到達した時点で開始される。ブロック電
池性能検知器30の手段としては、例えば開路電圧,内
部抵抗,ガスリーク率あるいはガスクロスを検知するた
めの燃料ガス中のO2濃度又は酸化剤ガス中のH2濃度
などが挙げられる。これらのうちの少なくとも1つの信
号の値を監視し、その設定値に到達すると電解質供給指
令装置31の指令により溶融した電解質が該積層型燃料
電池本体の外部からブロック電池用電解質供給装置32
により電解質分配容器18に供給される。電解質の供給
方法としてはガス配管,検知用端子,電流取出端子,電
解質供給用配管や電解質受用ホッパー等を格納するベル
ジャの外側から溶融した状態で供給することもできる
し、又所定量の電解質を固体状態で供給し、ベルジャ内
で溶融して電解質分配容器18に供給することもでき
る。電解質の供給は上記のごとく、電池運転状態のまま
実施できるが、他の方法としては電池運転を停止して降
温した状態、たとえば定検時にブロック電池性能検知器
30の検知信号の電池停止直前の値を基準にして、前記
ガスヘッダ8中空部の該電解質分配容器18から分岐し
た各単位電池用電解質溜20に所定量の電解質を固体状
態で供給することもできる。FIG. 4 shows an embodiment in which the performance of each unit battery is detected and an electrolyte is supplied if necessary. The contents of this embodiment will be described below with reference to FIG. The supply of the electrolyte is started when the set value of the signal is reached based on the magnitude of various signals that can detect the lack of the electrolyte. Examples of means of the block battery performance detector 30 include an open circuit voltage, an internal resistance, a gas leak rate or an O 2 concentration in a fuel gas or an H 2 concentration in an oxidant gas for detecting a gas cross. The value of at least one of these signals is monitored, and when the set value is reached, the electrolyte melted according to a command from the electrolyte supply command device 31 is supplied from the outside of the laminated fuel cell main body to the block battery electrolyte supply device 32.
Is supplied to the electrolyte distribution container 18. The electrolyte can be supplied in the molten state from the outside of the bell jar that houses the gas pipe, the detection terminal, the current extraction terminal, the electrolyte supply pipe, the electrolyte receiving hopper, etc., or a predetermined amount of electrolyte can be supplied. It is also possible to supply in a solid state, melt in the bell jar, and supply to the electrolyte distribution container 18. As described above, the supply of the electrolyte can be performed while the battery is operating, but another method is to stop the battery operation and lower the temperature, for example, just before stopping the battery of the detection signal of the block battery performance detector 30 at the time of regular inspection. Based on the value, it is also possible to supply a predetermined amount of electrolyte in a solid state to each unit battery electrolyte reservoir 20 branched from the electrolyte distribution container 18 in the hollow portion of the gas header 8.
上記の説明は電池スタックの各ブロックごとに前記信号
を検知し、ブロック単位で電解質の補給を実施する方法
であるが、場合によっては第4図に示すように1ブロッ
ク内の各単位電池の信号を検知し、ブロック内の特定の
単位電池のみに電解質を補給することも本発明の積層型
燃料電池においては可能である。詳細な手順は第3図の
ブロック電池の場合と同様であるので省略するがこの方
法を実施する場合には、1ブロックに積層された単位電
池の数に相当する複数本の電解質供給配管24を前記ガ
スヘッダ8内中央部にある電解質溜20上部に誘導して
おき、前記信号を検知してその設定値に到達したセルに
のみ電解液を補給できる。The above description is a method of detecting the signal for each block of the battery stack and performing electrolyte replenishment in block units, but in some cases, as shown in FIG. 4, the signal of each unit battery in one block is It is also possible in the laminated fuel cell of the present invention to detect the temperature and supply the electrolyte only to a specific unit cell in the block. The detailed procedure is the same as in the case of the block battery of FIG. 3 and therefore omitted, but when this method is carried out, a plurality of electrolyte supply pipes 24 corresponding to the number of unit batteries stacked in one block are provided. The electrolyte can be replenished only to the cells that reach the set value by detecting the signal by guiding the gas to the upper part of the electrolyte reservoir 20 in the center of the gas header 8.
電解質はその所定量を一度に全部供給することも可能で
あり、また一定の間隔をおいて分割供給することもでき
る。The electrolyte can be supplied at a predetermined amount all at once, or can be dividedly supplied at regular intervals.
第1〜第3の実施例の最も特徴とするところは、補給す
べき電解質を積層型燃料電池の上部においてほぼ均等に
分配し、それをそれぞれ各単位電池毎に独立して設けら
れた電解質通路を通して各単位電池毎に確実に電解質を
補給できることである。本実施例の方法によって、各単
位電池に均等に電解質を補給でき、また従来技術の方法
において起こり得る液短絡も防止できる。The most characteristic feature of the first to third embodiments is that the electrolyte to be replenished is distributed almost evenly in the upper part of the stacked fuel cell, and the electrolyte passages are provided independently for each unit cell. That is, the electrolyte can be surely replenished for each unit battery. According to the method of the present embodiment, the electrolyte can be evenly supplied to each unit cell, and the liquid short circuit which can occur in the conventional method can be prevented.
本発明によれば燃料電池のそれぞれの電解質マトリクス
基板にそれぞれ単独に適宜電解質導入路を通して電解質
を供給するので、液短絡の可能性が著しく少なくなりま
た、単位電池間の出力バラツキを小さくできるので、電
池の信頼性向上と稼動率の向上が可能となる。さらに電
池性能の長期安定化が図れるという優れた効果もある。According to the present invention, the electrolyte is supplied to each electrolyte matrix substrate of the fuel cell independently through the electrolyte introduction path, so that the possibility of liquid short circuit is significantly reduced, and the output variation between the unit cells can be reduced. It is possible to improve the reliability and operating rate of the battery. Further, there is an excellent effect that the battery performance can be stabilized for a long period of time.
【図面の簡単な説明】 第1図は本発明の一実施例を示す燃料電池の断面図、第
2図は第1図のA−A′断面図、第3図及び第4図は電
解質供給装置を表わすブロック図、第5図はブロック電
池を積重ねたときの斜視図、第6図はマルチセルの概念
を表わす斜視図である。 1…燃料極、2…酸化剤極、3…電解質マトリクス基
板、8…上部ガスヘッダ、9…下部ガスヘッダ、18…
電解質分配容器、20…電解質溜、24…電解質導入
路、30…ブロック電池性能検知器、31…電解質供給
指令装置、32…ブロック電池用電解質供給装置、40
…単位電池性能検知器、41…電解質供給指令装置、4
2…単位電池用電解質供給装置。BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a cross-sectional view of a fuel cell showing an embodiment of the present invention, FIG. 2 is a cross-sectional view taken along the line AA ′ of FIG. 1, and FIGS. FIG. 5 is a block diagram showing the device, FIG. 5 is a perspective view when the block batteries are stacked, and FIG. 6 is a perspective view showing the concept of the multi-cell. DESCRIPTION OF SYMBOLS 1 ... Fuel electrode, 2 ... Oxidizer electrode, 3 ... Electrolyte matrix substrate, 8 ... Upper gas header, 9 ... Lower gas header, 18 ...
Electrolyte distribution container, 20 ... Electrolyte reservoir, 24 ... Electrolyte introduction path, 30 ... Block battery performance detector, 31 ... Electrolyte supply command device, 32 ... Block battery electrolyte supply device, 40
... Unit battery performance detector, 41 ... Electrolyte supply command device, 4
2 ... Electrolyte supply device for unit battery.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 三次 浩一 茨城県日立市久慈町4026番地 株式会社日 立製作所日立研究所内 (72)発明者 岩瀬 嘉男 茨城県日立市久慈町4026番地 株式会社日 立製作所日立研究所内 (72)発明者 黒江 聡 茨城県日立市久慈町4026番地 株式会社日 立製作所日立研究所内 (72)発明者 加茂 友一 茨城県日立市久慈町4026番地 株式会社日 立製作所日立研究所内 (56)参考文献 特開 昭60−241659(JP,A) 特開 昭61−227370(JP,A) 特開 昭62−115668(JP,A) 特開 昭61−156637(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Koichi Miyoshi 4026 Kuji Town, Hitachi City, Ibaraki Prefecture Hitate Works Ltd., Hitachi Research Laboratory (72) Inventor Yoshio Iwase 4026 Kuji Town, Hitachi City, Ibaraki Prefecture Hitate Works Co., Ltd. Hitachi Research Laboratory (72) Inventor Satoshi Kuroe 4026 Kuji Town, Hitachi City, Ibaraki Prefecture, Hitate Works, Ltd. Hitachi Research Laboratory (72) Inventor Yuichi Kamo 4026 Kuji Town, Hitachi City, Ibaraki Prefecture, Hitachi Research Institute, Ltd. (56) References JP-A-60-241659 (JP, A) JP-A-61-227370 (JP, A) JP-A-62-115668 (JP, A) JP-A-61-156637 (JP, A)
Claims (6)
ス基板より小面積の一対の電極で挟持してなる単位電池
を前記電解質マトリクス基板と略同面積のセパレータを
介して複数積層した積層体と、前記積層体の上部に設け
られ各単位電池に反応ガスを給排する上部ガスヘッダと
を備えるブロック電池を含み、前記セパレータは前記各
電極に面して反応ガス流通路を備えると共に前記各電極
の周囲に前記電解質マトリクス基板と接するウエットシ
ール部を有する燃料電池において、 外部から電解質が供給される電解質分配容器と、該電解
質分配容器に連通する複数の電解質溜と、前記各電解質
溜と前記各電解質マトリクス基板とを連通する前記電解
質マトリクス基板と同数の電解質導入管とを備え、前記
上部ガスヘッダは前記電極を挟んで対向するウエットシ
ール部の上方部分に反応ガス供給部及び反応ガス排出部
を有すると共に該反応ガス供給部及び反応ガス排出部の
中間部分に反応ガスが流通しない領域を有し、前記電解
質分配容器及び電解質溜は前記上部ガスヘッダの反応ガ
スが流通しない領域に配置され、前記電解質導入管は前
記ウエットシール部を貫通し該ウエットシール部におい
て個別の電解質マトリクス基板を終端として配置されて
いることを特徴とする燃料電池。1. A laminate in which a plurality of unit batteries, each of which has an electrolyte matrix substrate sandwiched by a pair of electrodes having an area smaller than that of the electrolyte matrix substrate, are laminated with a separator having substantially the same area as the electrolyte matrix substrate interposed therebetween, and the laminate. A block battery having an upper gas header provided on the upper part of the body and supplying / discharging reaction gas to / from each unit battery, wherein the separator is provided with a reaction gas flow passage facing the electrodes and is provided around the electrodes. In a fuel cell having a wet seal part in contact with an electrolyte matrix substrate, an electrolyte distribution container to which an electrolyte is supplied from the outside, a plurality of electrolyte reservoirs communicating with the electrolyte distribution container, the electrolyte reservoirs and the electrolyte matrix substrates. And the same number of electrolyte introducing tubes as the electrolyte matrix substrate communicating with each other, and the upper gas header is paired with the electrode sandwiched therebetween. The reaction gas supply part and the reaction gas discharge part are provided in the upper part of the facing wet seal part, and the reaction gas supply part and the reaction gas discharge part have a region where the reaction gas does not flow in the intermediate part, and the electrolyte distribution container and The electrolyte reservoir is arranged in a region where the reaction gas of the upper gas header does not flow, and the electrolyte introduction pipe penetrates through the wet seal portion and is arranged in the wet seal portion by terminating the individual electrolyte matrix substrate. Fuel cell to do.
とを特徴とする特許請求の範囲第1項記載の燃料電池。2. The fuel cell according to claim 1, wherein a plurality of the block cells are stacked.
形成されていることを特徴とする特許請求の範囲第1項
または第2項記載の燃料電池。3. The fuel cell according to claim 1, wherein a plurality of unit cells are formed in the same separator surface.
ス基板より小面積の一対の電極で挟持してなる単位電池
を前記電解質マトリクス基板と略同面積のセパレータを
介して複数積層した積層体と、前記積層体の上部に設け
られ各単位電池に反応ガスを給排する上部ガスヘッダと
を備えるブロック電池を含み、前記セパレータは前記各
電極に面して反応ガス流通路を備えると共に前記各電極
の周囲に前記電解質マトリクス基板と接するウエットシ
ール部を有する燃料電池において、 電解質供給手段と、該電解質供給手段から電解質が供給
される電解質分配容器と、該電解質分配容器に連通する
複数の電解質溜と、前記各電解質溜と前記各電解質マト
リクス基板とを連通する前記電解質マトリクス基板と同
数の電解質導入管と、前記ブロック電池の発電性能を検
知するブロック電池性能検知手段と、前記ブロック電池
性能検知手段の検知信号により前記電解質供給手段に電
解質供給指令を出力する電解質供給指令手段とを備え、
前記上部ガスヘッダは前記電極を挟んで対向するウエッ
トシール部の上方部分に反応ガス供給部及び反応ガス排
出部を有すると共に該反応ガス供給部及び反応ガス排出
部の中間部分に反応ガスが流通ないし領域を有し、前記
電解質分配容器及び電解質溜は前記上部ガスヘッダの反
応ガスが流通しない領域に配置され、前記電解質導入管
は前記ウエットシール部を貫通し該ウエットシール部に
おいて個別の電解質マトリクス基板を終端として配置さ
れていることを特徴とする燃料電池。4. A laminate in which a plurality of unit cells, each of which has an electrolyte matrix substrate sandwiched by a pair of electrodes having a smaller area than the electrolyte matrix substrate, are laminated with a separator having substantially the same area as the electrolyte matrix substrate interposed therebetween, and the laminate. A block battery having an upper gas header provided on the upper part of the body and supplying / discharging reaction gas to / from each unit battery, wherein the separator is provided with a reaction gas flow passage facing the electrodes and is provided around the electrodes. In a fuel cell having a wet seal part in contact with an electrolyte matrix substrate, an electrolyte supply means, an electrolyte distribution container to which an electrolyte is supplied from the electrolyte supply means, a plurality of electrolyte reservoirs communicating with the electrolyte distribution container, and each of the electrolytes. Reservoirs and the electrolyte matrix substrates, the same number of electrolyte introduction tubes as the electrolyte matrix substrates, and the block electrodes. Block battery performance detection means for detecting the power generation performance of the pond, and an electrolyte supply command means for outputting an electrolyte supply command to the electrolyte supply means by a detection signal of the block battery performance detection means,
The upper gas header has a reaction gas supply part and a reaction gas discharge part in an upper part of the wet seal part facing each other with the electrode sandwiched therebetween, and a reaction gas flows or a region in an intermediate part between the reaction gas supply part and the reaction gas discharge part. And the electrolyte distribution container and the electrolyte reservoir are arranged in a region of the upper gas header where the reaction gas does not flow, and the electrolyte introduction pipe penetrates the wet seal portion and terminates an individual electrolyte matrix substrate in the wet seal portion. A fuel cell characterized by being arranged as.
とを特徴とする特許請求の範囲第4項記載の燃料電池。5. The fuel cell according to claim 4, wherein a plurality of the block cells are stacked.
形成されていることを特徴とする特許請求の範囲第4項
または第5項記載の燃料電池。6. The fuel cell according to claim 4 or 5, wherein a plurality of unit cells are formed in the same separator surface.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62240751A JPH0652667B2 (en) | 1987-09-28 | 1987-09-28 | Fuel cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62240751A JPH0652667B2 (en) | 1987-09-28 | 1987-09-28 | Fuel cell |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6484577A JPS6484577A (en) | 1989-03-29 |
| JPH0652667B2 true JPH0652667B2 (en) | 1994-07-06 |
Family
ID=17064166
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62240751A Expired - Fee Related JPH0652667B2 (en) | 1987-09-28 | 1987-09-28 | Fuel cell |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0652667B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2792626B2 (en) * | 1987-11-04 | 1998-09-03 | 三菱電機株式会社 | Fuel cell device and electrolyte replenishing method therefor |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60241659A (en) * | 1984-05-16 | 1985-11-30 | Agency Of Ind Science & Technol | Fused salt type fuel cell |
| JPH0624127B2 (en) * | 1984-06-12 | 1994-03-30 | 株式会社日立製作所 | How to operate a fuel cell |
| JPS61156637A (en) * | 1984-12-27 | 1986-07-16 | Sanyo Electric Co Ltd | Method of supplying electrolytic solution to fuel cell |
| US4572876A (en) * | 1985-04-01 | 1986-02-25 | Westinghouse Electric Corp. | Apparatus for supplying electrolyte to fuel cell stacks |
| JPS62115668A (en) * | 1985-11-13 | 1987-05-27 | Mitsubishi Electric Corp | Electrolyte supplement equipment of fuel cell |
-
1987
- 1987-09-28 JP JP62240751A patent/JPH0652667B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6484577A (en) | 1989-03-29 |
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