JPH0697617B2 - Molten carbonate fuel cell - Google Patents
Molten carbonate fuel cellInfo
- Publication number
- JPH0697617B2 JPH0697617B2 JP61031306A JP3130686A JPH0697617B2 JP H0697617 B2 JPH0697617 B2 JP H0697617B2 JP 61031306 A JP61031306 A JP 61031306A JP 3130686 A JP3130686 A JP 3130686A JP H0697617 B2 JPH0697617 B2 JP H0697617B2
- Authority
- JP
- Japan
- Prior art keywords
- electrode
- fuel
- molten carbonate
- wet seal
- 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 - Lifetime
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
- H01M8/0271—Sealing or supporting means around electrodes, matrices or membranes
-
- 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
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0206—Metals or alloys
-
- 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
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0206—Metals or alloys
- H01M8/0208—Alloys
- H01M8/021—Alloys based on iron
-
- 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
- H01M8/0247—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the form
-
- 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
- H01M8/14—Fuel cells with fused electrolytes
- H01M2008/147—Fuel cells with molten carbonates
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2300/00—Electrolytes
- H01M2300/0017—Non-aqueous electrolytes
- H01M2300/0048—Molten electrolytes used at high temperature
- H01M2300/0051—Carbonates
-
- 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〕 この発明は、溶融炭酸塩型燃料電池の構造に関するもの
である。The present invention relates to the structure of a molten carbonate fuel cell.
従来の溶融炭酸塩型燃料電池を第8図に示す。図におい
て、(1)、(2)はそれぞれ燃料ガス及び酸化剤ガス
供給用マニホールドである。第9図はマニホールド
(1)、(2)を外した状態を示す斜視図である。図に
おいて、(3)はセパレータ板で、燃料電極(6)に対
向して設ける燃料ガス流路と、酸化剤電極(7)に対向
して設ける酸化剤ガス流路を分離している。燃料ガス流
路と酸化剤ガス流路にはそれぞれ流路板(4)、(5)
が設けられている。燃料電極(6)と酸化剤電極(7)
は電解質層(8)を介在して対向し、単電池を構成して
いる。この燃料電極(6)は、例えばニツケルの多孔質
板で形成され、酸化剤電極(7)は、例えばNiOの多孔
体で形成されている。(9)は酸化剤電極(7)を保持
し、発生した電流を通過せしめる集電板、(10)は上端
板、(11)は下端板、(12)、(13)はそれぞれセパレ
ータ板(3)に設けられ、電池の内外を分離シールする
燃料側ウエツトシール部、及び酸化剤側ウエツトシール
部である。溶融炭酸塩型燃料電池は、単電池とセパレー
タ板(3)を交互に積層して形成される積層体で、上下
端には端板(10)、(11)が設けられている。第10図
は、セパレータ板(3)を示す斜視図で、例えば金属の
平板で形成されたウエツトシール部(12)、(13)がセ
パレータ板(3)のセパレータ部(3a)に接合されてい
る。マニホールド対向部(12a),(13a)はそれぞれマ
ニホールド(1)、(2)と接触し、反応ガスが電池外
部へ流出するのを防止している。A conventional molten carbonate fuel cell is shown in FIG. In the figure, (1) and (2) are manifolds for supplying fuel gas and oxidant gas, respectively. FIG. 9 is a perspective view showing a state in which the manifolds (1) and (2) are removed. In the figure, (3) is a separator plate, which separates the fuel gas channel provided facing the fuel electrode (6) and the oxidant gas channel provided facing the oxidant electrode (7). Flow passage plates (4) and (5) are provided in the fuel gas passage and the oxidant gas passage, respectively.
Is provided. Fuel electrode (6) and oxidizer electrode (7)
Are opposed to each other with the electrolyte layer (8) interposed therebetween to form a unit cell. The fuel electrode (6) is formed of, for example, a nickel porous plate, and the oxidant electrode (7) is formed of, for example, a NiO porous body. (9) is a current collector plate that holds the oxidant electrode (7) and allows the generated current to pass therethrough, (10) is an upper end plate, (11) is a lower end plate, and (12) and (13) are separator plates ( The fuel side wet seal portion and the oxidant side wet seal portion, which are provided in 3) and separate and seal the inside and outside of the cell. The molten carbonate fuel cell is a laminate formed by alternately stacking unit cells and separator plates (3), and end plates (10) and (11) are provided at the upper and lower ends. FIG. 10 is a perspective view showing the separator plate (3). For example, the wet seal parts (12) and (13) formed of a metal flat plate are joined to the separator part (3a) of the separator plate (3). . The manifold facing portions (12a) and (13a) are in contact with the manifolds (1) and (2), respectively, and prevent the reaction gas from flowing out of the battery.
次に、この種の溶融炭酸塩型燃料電池の動作について説
明する。燃料電池は、燃料ガス供給用マニホールド
(1)から供給される水素などの燃料ガスと、酸化剤ガ
ス供給用マニホールド(2)から供給される空気などの
酸化剤ガスの持つ化学エネルギーを、電気化学的な反応
によつて直接電気エネルギーに変換し、電力を得る装置
である。この電気化学反応を効率良く行なわせるため
に、一般には多孔質な電極(6)、(7)が使われる。Next, the operation of this type of molten carbonate fuel cell will be described. The fuel cell uses the chemical energy of the fuel gas such as hydrogen supplied from the fuel gas supply manifold (1) and the chemical energy of the oxidant gas such as air supplied from the oxidant gas supply manifold (2) to be electrochemically converted. It is a device that obtains electric power by directly converting into electrical energy by a dynamic reaction. In order to efficiently carry out this electrochemical reaction, generally porous electrodes (6) and (7) are used.
燃料電極(6)及び酸化剤電極(7)における反応は次
の通りである。The reactions at the fuel electrode (6) and the oxidant electrode (7) are as follows.
燃料電極 H2+▲CO2- 3▼→H2O+CO2+2a …(1) 酸化剤電極 CO2+1/2O2+2e→▲CO2- 3▼ …(2) 燃料電極では、式(1)の様に、燃料ガス流路を流れる
燃料ガス中のH2は電解質中の▲CO2- 3▼と反応し、水とC
O2と電子を生成する。この電子は、燃料電極(6)を通
して外部負荷に送られた後、酸化剤電極(7)に流れこ
む。酸化剤電極(7)では、この電子とCO2及び酸化剤
ガス流路を流れる酸化剤ガス中のO2から▲CO2- 3▼を生
成し、電解質層(8)中に溶解することによつて電池反
応が進行する。The fuel electrode H 2 + ▲ CO 2- 3 ▼ → H 2 O + CO 2 + 2a ... (1) oxidizer electrode CO 2 + 1 / 2O 2 + 2e → ▲ CO 2- 3 ▼ ... (2) In the fuel electrode, equation (1) as in, H 2 in the fuel gas flowing through the fuel gas passage is reacted with ▲ CO 2- 3 ▼ in the electrolyte, water and a C
Generates O 2 and electrons. After being sent to the external load through the fuel electrode (6), the electrons flow into the oxidant electrode (7). In the oxidant electrode (7), that this generates electrons and CO 2 and the oxidant gas flow path from O 2 in the oxidizing gas flowing ▲ CO 2- 3 ▼, dissolved in the electrolyte layer (8) Therefore, the battery reaction proceeds.
上記のような溶融炭酸塩型燃料電池のウエツトシール部
(12)、(13)は金属平板により形成されており、柔軟
性がないため、電極(6)、(7)の厚さの設計が不適
当であると、電解質層(8)、電極(6)、(7)など
が接触不良を起したり、反応ガスが漏れたりする。ま
た、電池の運転時間の経過と共に電極(6)、(7)が
薄くなつた場合にも、電極(6)、(7)の両端に配置
されているウエツトシール部(12)、(13)は変形しな
いため、やはり接触不良により電池の内部抵抗が増加す
るという問題点があつた。Since the wet seal parts (12) and (13) of the molten carbonate fuel cell as described above are formed of a metal flat plate and have no flexibility, the thickness design of the electrodes (6) and (7) is unsatisfactory. If appropriate, the electrolyte layer (8), the electrodes (6), (7), etc. may cause poor contact or the reaction gas may leak. Further, even when the electrodes (6) and (7) become thin with the lapse of operating time of the battery, the wet seal parts (12) and (13) arranged at both ends of the electrodes (6) and (7) are Since it does not deform, there is a problem that the internal resistance of the battery increases due to poor contact.
このような問題点を解決する溶融炭酸塩型燃料電池とし
て、USP 4514475号に掲載されたものの部分斜視図を第1
1図に示し、セパレータ板の斜視図を第12図に示す。図
において、(14)はセパレータ板で、第13図に示すよう
な金属板の四隅を四角形に切り取り、矢印で示すように
燃料ガス流路に平行な対向する二辺(12b)を燃料電極
側、即ち紙面の表側に折り返し、酸化剤ガス流路に平行
な対向する二辺(13b)を酸化剤電極側、即ち紙面の裏
側に折り返して、ウエツトシール部(12)、(13)を形
成して第12図に示すセパレータ板(14)を構成したもの
である。この折り返し辺(12b)、(13b)の内側には、
ウエツトシール部を保持するため、第14図に示すスペー
サ(15)が配置されている。このような構成の溶融炭酸
塩型燃料電池のウエツトシール部(12)、(13)は柔軟
性があり、電極(6)、(7)や電解質層(8)などの
接触を良好に保つことができ、このため、電池の内部抵
抗の増加をおさえることができる。ところが、マニホー
ルド(1)、(2)を取り付けた際、ウエツトシール部
(12)、(13)のマニホールド対向部(12a),(13a)
の全面をマニホールド(1)、(2)が被うように構成
するのが困難である。このため、ガスシール性が悪く、
このマニホールド対向部(12a),(13a)からガスがも
れて、電池特性が低下するという欠点があつた。As a molten carbonate fuel cell that solves such problems, a partial perspective view of the one disclosed in USP 4514475 is shown in FIG.
It is shown in FIG. 1 and a perspective view of the separator plate is shown in FIG. In the figure, (14) is a separator plate, and the four corners of the metal plate as shown in FIG. 13 are cut into quadrangles, and the two opposite sides (12b) parallel to the fuel gas flow path are shown on the fuel electrode side as shown by arrows. That is, it is folded back to the front side of the paper surface, and two opposite sides (13b) parallel to the oxidant gas flow path are folded back to the oxidant electrode side, that is, the back side of the paper surface to form the wet seal parts (12) and (13). This is a constitution of the separator plate (14) shown in FIG. Inside the folded sides (12b) and (13b),
A spacer (15) shown in FIG. 14 is arranged to hold the wet seal portion. The wet seal parts (12) and (13) of the molten carbonate fuel cell having such a structure are flexible and can keep good contact with the electrodes (6) and (7) and the electrolyte layer (8). Therefore, the internal resistance of the battery can be prevented from increasing. However, when the manifolds (1) and (2) are attached, the wet seal parts (12) and (13) face the manifolds (12a) and (13a).
It is difficult to cover the entire surface of the manifold with the manifolds (1) and (2). Therefore, the gas sealability is poor,
The gas leaks from the manifold facing portions (12a) and (13a), and the battery characteristics are deteriorated.
従来の溶融炭酸塩型燃料電池は以上のように構成されて
いるので、ウエツトシール部に柔軟性がなく、電極の厚
さ設計が不適当であると電解質層や電極などが接触不良
を起こしたり、反応ガスが漏れたりする。また、電池の
運転時間の経過と共に電極が薄くなつた場合、ウエツト
シール部はこの変形に追随しないため、やはり接触不良
により電池の内部抵抗が増加するという問題点があつ
た。Since the conventional molten carbonate fuel cell is configured as described above, the wet seal portion is not flexible, and if the thickness design of the electrode is improper, the electrolyte layer, the electrode, or the like may cause poor contact, Reaction gas leaks. Further, when the electrode becomes thin with the lapse of operating time of the battery, the wet seal portion does not follow this deformation, so that there is a problem that the internal resistance of the battery increases due to poor contact.
また、ウエツトシール部に柔軟性を持たせた構造の溶融
炭酸塩型燃料電池では、ガスシールが完全でなく、ウエ
ツトシール部のマニホールド対向部からガスが漏れ、電
池特性の低下を招くなどの問題点があつた。In addition, in the molten carbonate fuel cell having a structure in which the wet seal portion has flexibility, there is a problem that the gas seal is not perfect and gas leaks from the portion of the wet seal portion facing the manifold, resulting in deterioration of cell characteristics. Atsuta
この発明は上記のような従来のものの問題点を解消する
ためになされたもので、電極や電解質の接触不良を低下
し、電極が薄くなつても内部抵抗が増加せず、かつ、ガ
スシール性を良好にして電池特性の高い溶融炭酸塩型燃
料電池を提供することを目的としている。The present invention has been made to solve the problems of the conventional ones described above, reduces the contact failure of the electrode and the electrolyte, does not increase the internal resistance even when the electrode is thin, and gas sealability It is an object of the present invention to provide a molten carbonate fuel cell having good cell characteristics and high cell characteristics.
〔問題点を解決するための手段〕 この発明に係る溶融炭酸塩型燃料電池は、セパレータ板
を構成する金属板の燃料ガス流路に平行な対向する二辺
を燃料電極側に、酸化剤ガス流路に平行な対向する二辺
を酸化剤電極側にそれぞれ折り返し、この折り返しで形
成された折り返し部両端のマニホールド対向部の折り返
し片先端側を除いてコーナー部側に薄い金属板を接合
し、マニホールド対向部のコーナー部側を密閉すると共
に平坦してウエツトシール部を構成し、さらにセパレー
タ板はウエツトシール部の折り返し片が電解質層に接す
るようにセパレータ板を積層したものである。[Means for Solving the Problems] In a molten carbonate fuel cell according to the present invention, two opposing sides of a metal plate forming a separator plate, which are parallel to a fuel gas flow path, are on the fuel electrode side, and an oxidizer gas is provided. Two opposite sides parallel to the flow path are folded back to the oxidizer electrode side, and a thin metal plate is bonded to the corner portion side except the folded piece tip end side of the manifold facing portion at both ends of the folded portion formed by this folding, The corner portion side of the manifold facing portion is hermetically sealed and flattened to form a wet seal portion, and the separator plate is formed by laminating separator plates so that the folded pieces of the wet seal portion are in contact with the electrolyte layer.
この発明におけるウエツトシール部は、金属板を折り返
して形成されているため、柔軟性を有し、電極の厚さが
変動してもこれを吸収して電極や電解質層などの接触不
良を防ぐ。さらに、折り返し部両端のマニホールド対向
部の折り返し片先端側を除いてコーナー部側にキャップ
を接合し、マニホールド対向部のコーナー部側を密閉す
ると共に平坦に構成したので、マニホールド対向部の折
り返し片がキャップの先端を支点として上下動可能とな
り、電極の厚さの変動をマニホールド対向部においても
吸収して電極や電解質などの接触不良を防ぎ、ウエツト
シール部のマニホールド対向部及びマニホールドとウエ
ツトシール部の間からガスが漏れるのを防ぐ。Since the wet seal portion in the present invention is formed by folding back the metal plate, it has flexibility and absorbs the variation in the thickness of the electrode to prevent the contact failure of the electrode or the electrolyte layer. Furthermore, since the cap is joined to the corner side except the tip of the folded piece of the manifold facing portion at both ends of the folded portion to seal the corner side of the manifold facing portion and to make it flat, the folded piece of the manifold facing portion is It can move up and down with the tip of the cap as a fulcrum, absorbs fluctuations in the electrode thickness even in the manifold facing part to prevent contact failure of electrodes and electrolytes, etc. from the manifold facing part of the wet seal part and between the manifold and the wet seal part. Prevent gas from leaking.
以下、この発明の一実施例を図について説明する。第1
図において、(14)はセパレータ板、(16)はウエツト
シール部(12)、(13)のそれぞれマニホールド対向部
(12a)、(13a)に接合されたキヤツプである。セパレ
ータ板(14)は例えば0.1〜1.0mmの厚さのニツケルとス
テンレス(例えばSUS 316L、又はSUS 310s)のクラツド
板で、ニツケルの厚さの比は耐腐食性などを考慮して1/
9〜1/6程度のもので形成される。クラツド板を第13図の
ように、燃料ガス流路に平行な対向する二辺(12b)を
燃料電極側、即ち紙面の表側に折り返し、燃料ガス流路
と直交して設けられている酸化剤ガス流路に平行な二辺
(13b)を酸化剤電極側、即ち紙面の裏側に折り返して
第2図のように、折り返し片(12b)、(13b)がそれぞ
れセパレータ板(14)に対向して、かつ、平行に形成さ
れている。そして、この折り返し片(12b)、(13b)が
それぞれウエツトシール部(12)、(13)を形成し、耐
腐食性からニッケル面が燃料ガス流路に対向し、かつ、
折り返し片(12b)、(13b)が電解質層(8)を接する
ようにセパレータ板(14)が積層されている。さらに、
折り返しで構成された折り返し部のマニホールド対向部
(12a)、(13a)に、折り返し片(12b)、(13b)の先
端部側を除いて弧状端部側、即ちコーナー部側を密閉す
ると共に平坦にするためのキヤツプ(16)を接合してい
る。キヤツプ(16)は例えば第3図に示すような形状
で、0.05〜1mm程度の厚さのニツケルとステンレス(例
えばSUSU 316L、又はSUS 310s)のクラツド板で形成さ
れ、第2図に示すようにマニホールド対向部(12a)、
(13a)にはめ込み、プラズマアーク溶接法などにより
周囲を溶接したものである。このキヤツプ(16)はマニ
ホールド対向部(12a)、(13a)の例えば真中からコー
ナー部側を密閉するように構成されており、ウエツトシ
ール部(12)、(13)をある程度保持すると共に、キヤ
ツプ(16)の形成されていないマニホールド対向部(12
a)、(13a)及びウエツトシール部(12)、(13)の中
央部は柔軟性を有し、電極(6)、(7)の厚さが設計
不適当な時にも電極(6)、(7)及び電解質層(8)
などの接触不良を防ぐ。さらに、電池の運転時間が経過
するにつれて電極(6)、(7)の厚さが50μm〜100
μm程度減つても、これに応じて中央部においては折り
返し片(12a)、(13a)全体が、ある程度下がり、コー
ナー部においては中途から自由端にかけての折り返し片
(12a)、(13a)が中途点を支点にしてある程度下が
り、電極(6)、(7)及び電解質層(8)などの接触
不良や、反応ガスのもれを防ぐ。従つて内部抵抗の増加
を防ぐ。また、マニホールド対向部(12a)、(13a)
に、マニホールド(1)、(2)を取り付けた状態にお
いては、ウエツトシール部(12)、(13)のコーナー部
は密閉されているため、ガス流路が密閉でき、ガスシー
ル性が良好となる。さらにマニホールド対向部(12
a)、(13a)は平坦に構成されており、マニホールド
(1)、(2)の取付面と密着してこの間に空間が生じ
ないため、この部分からのガスのもれも防ぐ高い電池特
性を得ることができる。An embodiment of the present invention will be described below with reference to the drawings. First
In the figure, (14) is a separator plate, and (16) is a cap joined to the manifold facing portions (12a) and (13a) of the wet seal portions (12) and (13), respectively. The separator plate (14) is, for example, a nickel-nickel plate having a thickness of 0.1 to 1.0 mm and a stainless steel plate (for example, SUS 316L or SUS 310s), and the nickel plate has a thickness ratio of 1/1/1 in consideration of corrosion resistance.
It is formed of 9 to 1/6. As shown in FIG. 13, the clad plate is folded back to the fuel electrode side, that is, the front side of the paper, with the two opposite sides (12b) parallel to the fuel gas passage, and the oxidizer provided orthogonally to the fuel gas passage. The two sides (13b) parallel to the gas flow path are folded back to the oxidizer electrode side, that is, the back side of the paper, and the folding pieces (12b) and (13b) face the separator plate (14) as shown in FIG. And are formed in parallel. The folded pieces (12b) and (13b) form the wet seal portions (12) and (13), respectively, and the nickel surface faces the fuel gas passage due to corrosion resistance, and
A separator plate (14) is laminated so that the folded back pieces (12b) and (13b) contact the electrolyte layer (8). further,
Flatten the arc-shaped end side, that is, the corner side, except for the tip side of the folded-back pieces (12b) and (13b), on the manifold facing portions (12a) and (13a) of the folded-back section, which are flat and sealed. The cap (16) for joining is joined. The cap (16) has, for example, a shape as shown in FIG. 3, and is formed of a nickel plate having a thickness of about 0.05 to 1 mm and a stainless steel (for example, SUSU 316L or SUS 310s) cladding plate, and as shown in FIG. Manifold facing part (12a),
It is fitted in (13a) and the periphery is welded by plasma arc welding or the like. The cap (16) is configured to seal, for example, the center of the manifold facing portions (12a) and (13a) to the corner portion side, holds the wet seal portions (12) and (13) to some extent, and also the cap (16). Manifold facing part (12)
a), (13a) and the central portions of the wet seal parts (12), (13) have flexibility, and the electrodes (6), (7) can be formed even when the thickness of the electrodes (6), (7) is inappropriate. 7) and electrolyte layer (8)
Prevents poor contact such as. Further, as the operating time of the battery elapses, the thickness of the electrodes (6) and (7) becomes 50 μm to 100 μm.
Even if it is reduced by about μm, the folded pieces (12a) and (13a) are lowered in the central portion to some extent, and the folded pieces (12a) and (13a) from the middle to the free end are halfway at the corners. The point serves as a fulcrum to lower to some extent to prevent contact failure of the electrodes (6) and (7) and the electrolyte layer (8) and leakage of reaction gas. Therefore, increase in internal resistance is prevented. Also, manifold facing parts (12a), (13a)
In the state where the manifolds (1) and (2) are attached, since the corner portions of the wet seal portions (12) and (13) are hermetically sealed, the gas flow passage can be hermetically sealed and the gas sealability is improved. . Manifold facing part (12
Since a) and (13a) are configured flat and have close contact with the mounting surfaces of the manifolds (1) and (2) and no space is created between them, high battery characteristics that prevent gas leakage from this part Can be obtained.
第4図は上端板(10)におけるウエツトシール部(13)
を示すもので、この場合は第5図に示す形状のキヤツプ
(16)を上下逆にしてマニホールド対向部(13a)に接
合して構成しており、下端板(11)に関しても同様であ
る。上記実施例では下端板(11)は燃料ガス流路に対向
しており、このキヤツプ(16)の燃料ガス流路との対向
面は、耐腐食性からニツケル面になるように構成し、上
端板(10)は酸化剤ガス流路に対向しているので、SUS
316L又はSUS 310Sの薄板で構成すればよい。第6図は上
記実施例に用いた燃料電極(6)を示すもので、折り返
し片(12b)とセパレータ板(14)との間に挿入される
両端部(6a)の厚さを折り返し片(12b)の厚さだけ薄
くしている。この実施例では折り返し片(12b)とセパ
レータ板(14)との間にこのような構造の燃料電極
(6)と燃料ガス流路を形成する流路板(4)を挿入し
て構成しているので、燃料電極(6)及び流路板(4)
がウエツトシール部(12)を保持するスペーサの働きを
すると共に電解質層(8)に対向する面が平らになる。
さらに、時間の経過に伴つたキヤツプ(16)の形成され
ていない折り返し片(12b)とセパレータ板(14)との
間に挿入された電極と電池中央部の電極とは同じ割合で
変形し、折り返し片(12b)の電極(6)と接触する部
分も電極(6)と離れることなく、ウエツトシール部
(12)と電極(6)面の高さが常に同じになる。さらに
電極(6)が折り返し片(12b)で保持されることにな
り、ずれなどを防止することもできる。以上のことは、
酸化剤側においても同様である。Fig. 4 shows the wet seal part (13) on the top plate (10).
In this case, the cap (16) having the shape shown in FIG. 5 is turned upside down and joined to the manifold facing portion (13a), and the lower end plate (11) is also the same. In the above embodiment, the lower end plate (11) is opposed to the fuel gas flow passage, and the surface of the cap (16) facing the fuel gas flow passage is configured to be a nickel surface due to corrosion resistance. Since the plate (10) faces the oxidant gas flow path, SUS
It may be composed of a thin plate of 316L or SUS 310S. FIG. 6 shows the fuel electrode (6) used in the above-mentioned embodiment, in which the thickness of both end portions (6a) inserted between the folded piece (12b) and the separator plate (14) is changed to the folded piece ( The thickness of 12b) is reduced. In this embodiment, the fuel electrode (6) having such a structure and the flow channel plate (4) forming the fuel gas flow channel are inserted between the folded piece (12b) and the separator plate (14). The fuel electrode (6) and the flow path plate (4)
Acts as a spacer for holding the wet seal part (12) and the surface facing the electrolyte layer (8) becomes flat.
Further, with time, the electrode inserted between the folded piece (12b) on which the cap (16) is not formed and the separator plate (14) and the electrode at the center of the battery deform at the same rate, The portion of the folded piece (12b) that comes into contact with the electrode (6) is not separated from the electrode (6), and the heights of the wet seal portion (12) and the surface of the electrode (6) are always the same. Further, the electrode (6) is held by the folded piece (12b), and it is possible to prevent misalignment. The above is
The same applies to the oxidant side.
セパレータ板(14)を構成する金属板は0.1〜1mm程度の
ものを用いており、0.1mm以下だと耐腐食性に問題があ
り、1mm以上だと柔軟性に問題がでてきる。特に好まし
くは0.1〜0.5mm程度がよい。また、同様にキヤツプ(1
6)を構成する金属板も耐腐食性と柔軟性の点から0.05
〜1mm程度のものを用い、特に0.1〜0.5mm程度のものが
好ましい。セパレータ板(14)及びキヤツプ(16)の材
質は、SUS 316L又はSUS 310Sのいずれか単独、あるいは
ニツケルとステンレス(例えばSUS 316L又はSUS 310S)
のクラツド板を用いることができる。ただし、燃料側に
用いるものは、耐腐食性から、ニツケル面であることが
望ましい。The metal plate constituting the separator plate (14) is about 0.1 to 1 mm, and if it is 0.1 mm or less, there is a problem in corrosion resistance, and if it is 1 mm or more, there is a problem in flexibility. Particularly preferably, it is about 0.1 to 0.5 mm. Similarly, the cap (1
The metal plate that constitutes 6) is also 0.05 in terms of corrosion resistance and flexibility.
Approximately 1 mm is used, and in particular approximately 0.1 mm to 0.5 mm is preferable. The material of the separator plate (14) and the cap (16) is either SUS 316L or SUS 310S alone, or nickel and stainless steel (eg SUS 316L or SUS 310S).
Clad boards can be used. However, it is desirable that the one used on the fuel side has a nickel surface because of its corrosion resistance.
第7図はこの発明の他の実施例に係るキヤツプ(16)を
示す斜視図であり、その側面部(16a)は波形状に構成
されている。このキヤツプ(16)を用いれば、上記効果
に加えてウエツトシール部(12)、(13)のコーナー部
における柔軟性が向上する。マニホールド対向部を平坦
にするために、波形状の凹部にペーストを入れると、柔
軟性を有し、かつマニホールド対向部が平坦なキヤツプ
(16)を実現できる。また、キヤツプ(16)と折り返し
てできる折り返し部のマニホールド対向部との接合方法
は、電気抵抗溶接、レーザ溶接、電子ビーム溶接、プラ
ズマアーク溶接、ろう付けなどで実現できる。FIG. 7 is a perspective view showing a cap (16) according to another embodiment of the present invention, the side surface (16a) of which is formed in a wavy shape. If this cap (16) is used, in addition to the above effects, the flexibility of the corner portions of the wet seal portions (12) and (13) is improved. When the paste is put in the corrugated concave portion to make the manifold facing portion flat, a cap (16) having flexibility and having a flat manifold facing portion can be realized. Further, the method of joining the cap (16) to the manifold facing portion of the folded portion that can be folded back can be realized by electric resistance welding, laser welding, electron beam welding, plasma arc welding, brazing, or the like.
以上のようにこの発明によれば、電解質層を介在して対
向する燃料電極と酸化剤電極を有する単電池、及び燃料
電極に対向して設ける燃料ガス流路と酸化剤電極に対向
して燃料ガス流路に直交して設ける酸化剤ガス流路とを
分離し、電池の内外を分離シールするウエツトシール部
を有するセパレータ板を交互に積層する積層体、並びに
燃料ガス流路と酸化剤ガス流路にそれぞれ燃料ガスと酸
化剤ガスを供給するマニホールドを備えた溶融炭酸塩型
燃料電池において、ウエツトシール部はセパレータ板を
構成する金属板の燃料ガス流路に平行な対向する二辺を
燃料電極側に、酸化剤ガス流路に平行な対向する二辺を
酸化剤電極側にそれぞれ折り返し、この折り返しで形成
された折り返し部両端のマニホールド対向部の折り返し
片先端側を除いてコーナー部側に薄い金属板を接合し、
マニホールド対向部のコーナー部側を密閉すると共に平
坦にして構成され、セパレータ板はウエツトシール部の
折り返し片が上記電解質層に接するように積層されてい
るので、電極の設計が不適当な時や電極が薄くなつても
内部抵抗の増加を防止でき、かつウエツトシール部のガ
スシール性を良好にし、電池特性の高い溶融炭酸塩型燃
料電池を提供できる効果がある。As described above, according to the present invention, a single cell having a fuel electrode and an oxidant electrode that face each other with an electrolyte layer interposed therebetween, and a fuel gas flow path that is provided to face the fuel electrode and a fuel that faces the oxidant electrode are provided. A laminated body in which a separator plate having a wet seal portion that separates and seals the inside and outside of the battery is separated from the oxidant gas flow path provided orthogonal to the gas flow path, and a fuel gas flow path and an oxidant gas flow path. In a molten carbonate fuel cell equipped with a manifold for supplying fuel gas and oxidant gas respectively, the wet seal part has two opposite sides parallel to the fuel gas flow path of the metal plate forming the separator plate on the fuel electrode side. , The two opposite sides parallel to the oxidant gas flow path are folded back toward the oxidant electrode side, except for the tip of the folded piece at the opposite end of the manifold formed by this fold. Joining thin metal plate Na side,
It is configured to seal and flatten the corner side of the manifold facing part, and the separator plate is laminated so that the folded piece of the wet seal part is in contact with the electrolyte layer, so when the electrode design is inappropriate or the electrode is Even if it is made thin, it is possible to prevent an increase in internal resistance, improve the gas sealability of the wet seal portion, and provide a molten carbonate fuel cell having high cell characteristics.
第1図はこの発明の一実施例による溶融炭酸塩型燃料電
池を示す斜視図、第2図はこの発明の一実施例に係るセ
パレータ板を示す斜視図、第3図は第2図に用いられた
キヤツプを示す斜視図、第4図はこの発明の一実施例に
係る端板を示す斜視図、第5図は第4図に用いられたキ
ヤツプを示す斜視図、第6図はこの発明の一実施例に係
る電極の斜視図、第7図はこの発明の他の実施例に係る
キヤツプを示す斜視図、第8図は一般的な溶融炭酸塩型
燃料電池にマニホールドを取り付けて示す斜視図、第9
図は従来の溶融炭酸塩型燃料電池を示す斜視図、第10図
は第9図に用いられたセパレータ板を示す斜視図、第11
図は他の従来の溶融炭酸塩型燃料電池の一部を示す部分
斜視図、第12図は第11図に用いられたセパレータ板を示
す斜視図、第13図は第11図に用いられたセパレータ板を
形成する金属板を示す平面図、第14図は第11図に用いら
れたスペーサを示す斜視図である。 (1)…燃料ガス供給用マニホールド、(2)…酸化剤
ガス供給用マニホールド、(4)…燃料ガス流路板、
(5)…酸化剤ガス流路板、(6)…燃料電極、(7)
…酸化剤電極、(8)…電解質層、(12)、(13)…ウ
エツトシール部、(12a)、(13a)…マニホールド対向
部、(12b)、(13b)…折り返し片、(14)…セパレー
タ板。 なお、図中、同一符号は同一、又は相当部分を示す。1 is a perspective view showing a molten carbonate fuel cell according to an embodiment of the present invention, FIG. 2 is a perspective view showing a separator plate according to an embodiment of the present invention, and FIG. 3 is used for FIG. 4 is a perspective view showing an end plate according to an embodiment of the present invention, FIG. 5 is a perspective view showing the cap used in FIG. 4, and FIG. 6 is a perspective view showing the cap used in FIG. FIG. 7 is a perspective view showing an electrode according to an embodiment of the present invention, FIG. 7 is a perspective view showing a cap according to another embodiment of the present invention, and FIG. 8 is a perspective view showing a manifold attached to a general molten carbonate fuel cell. Figure, No. 9
FIG. 10 is a perspective view showing a conventional molten carbonate fuel cell, FIG. 10 is a perspective view showing the separator plate used in FIG. 9, and FIG.
FIG. 12 is a partial perspective view showing a part of another conventional molten carbonate fuel cell, FIG. 12 is a perspective view showing a separator plate used in FIG. 11, and FIG. 13 is used in FIG. FIG. 14 is a plan view showing a metal plate forming a separator plate, and FIG. 14 is a perspective view showing a spacer used in FIG. (1) ... Manifold for supplying fuel gas, (2) ... Manifold for supplying oxidant gas, (4) ... Fuel gas flow path plate,
(5) ... Oxidant gas flow channel plate, (6) ... Fuel electrode, (7)
... oxidant electrode, (8) ... electrolyte layer, (12), (13) ... wet seal part, (12a), (13a) ... manifold facing part, (12b), (13b) ... folded piece, (14) ... Separator plate. In the drawings, the same reference numerals indicate the same or corresponding parts.
Claims (3)
化剤電極を有する単電池、及び燃料電極に対向して設け
る燃料ガス流路と酸化剤電極に対向して燃料ガス流路に
直交して設ける酸化剤ガス流路とを分離し、電池の内外
を分離シールするウエツトシール部を有するセパレータ
板を交互に積層する積層体、並びに燃料ガス流路と酸化
剤ガス流路にそれぞれ燃料ガスと酸化剤ガスを供給する
マニホールドを備えた溶融炭酸塩型燃料電池において、
上記ウエツトシール部は上記セパレータ板を構成する金
属板の燃料ガス流路に平行な対向する二辺を燃料電極側
に、酸化剤ガス流路に平行な対向する二辺を酸化剤電極
側にそれぞれ折り返し、この折り返しで形成された折り
返し部両端のマニホールド対向部の折り返し片先端側を
除いてコーナー部側に薄い金属板を接合し、上記マニホ
ールド対向部のコーナー部側を密閉すると共に平坦にし
て構成され、上記セパレータ板は上記ウエツトシール部
の折り返し片が上記電解質層に接するように積層されて
いることを特徴とする溶融炭酸塩型燃料電池。1. A unit cell having a fuel electrode and an oxidant electrode which face each other with an electrolyte layer interposed therebetween, and a fuel gas channel provided to face the fuel electrode and a fuel gas channel which faces the oxidant electrode and is orthogonal to the fuel gas channel. A laminate for alternately separating separator plates having a wet seal portion for separating and sealing the inside and outside of the battery, and a fuel gas in the fuel gas passage and the oxidizing gas passage, respectively. In a molten carbonate fuel cell equipped with a manifold supplying oxidant gas,
The wet seal portion is formed by folding back two opposite sides of the metal plate constituting the separator plate, which are parallel to the fuel gas flow path, to the fuel electrode side and two opposite sides parallel to the oxidant gas flow path to the oxidant electrode side. , A thin metal plate is joined to the corner portion side except the tip end side of the folded piece of the manifold facing portion at both ends of the folded portion formed by this folding, and the corner portion side of the manifold facing portion is hermetically sealed and flattened. The molten carbonate fuel cell is characterized in that the separator plate is laminated so that the folded piece of the wet seal portion is in contact with the electrolyte layer.
の折り返し片とセパレータ板との間に電極と流路板を挿
入したことを特徴とする特許請求の範囲第1項記載の溶
融炭酸塩型燃料電池。2. The molten carbonate fuel according to claim 1, wherein an electrode and a flow path plate are inserted between the folded piece of the wet seal portion formed by folding back and the separator plate. battery.
れた部分の電極を折り返し片の厚さだけ薄くしたことを
特徴とする特許請求の範囲第2項記載の溶融炭酸塩型燃
料電池。3. The molten carbonate fuel cell according to claim 2, wherein the electrode in the portion inserted between the folded piece and the separator plate is thinned by the thickness of the folded piece.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61031306A JPH0697617B2 (en) | 1986-02-14 | 1986-02-14 | Molten carbonate fuel cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61031306A JPH0697617B2 (en) | 1986-02-14 | 1986-02-14 | Molten carbonate fuel cell |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62188177A JPS62188177A (en) | 1987-08-17 |
| JPH0697617B2 true JPH0697617B2 (en) | 1994-11-30 |
Family
ID=12327606
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61031306A Expired - Lifetime JPH0697617B2 (en) | 1986-02-14 | 1986-02-14 | Molten carbonate fuel cell |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0697617B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20150058978A (en) * | 2013-11-21 | 2015-05-29 | 두산중공업 주식회사 | Cell package and fuel cell assembly having the same |
| KR20150066314A (en) * | 2013-12-06 | 2015-06-16 | 두산중공업 주식회사 | Cell package for fuel cell |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4689280A (en) * | 1986-02-20 | 1987-08-25 | Energy Research Corporation | Fuel cell stack end plate structure |
| JP2768698B2 (en) * | 1988-09-09 | 1998-06-25 | 三菱電機株式会社 | Internal manifold type molten carbonate fuel cell |
| US20050042494A1 (en) * | 2003-08-19 | 2005-02-24 | Chao-Yi Yuh | Compliant member for wet seal |
| KR100731329B1 (en) * | 2006-02-10 | 2007-06-21 | 두산중공업 주식회사 | Separation plate for molten carbonate fuel cell including fuel reforming chamber and manufacturing method thereof |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4514475A (en) * | 1984-03-30 | 1985-04-30 | The United States Of America As Represented By The United States Department Of Energy | Fuel cell separator with compressible sealing flanges |
-
1986
- 1986-02-14 JP JP61031306A patent/JPH0697617B2/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20150058978A (en) * | 2013-11-21 | 2015-05-29 | 두산중공업 주식회사 | Cell package and fuel cell assembly having the same |
| KR20150066314A (en) * | 2013-12-06 | 2015-06-16 | 두산중공업 주식회사 | Cell package for fuel cell |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62188177A (en) | 1987-08-17 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US20060024534A1 (en) | Fuel cell | |
| JPH1197039A (en) | Stacked fuel cell and method of manufacturing the same | |
| JP7186199B2 (en) | Electrochemical reaction cell stack | |
| JPS5893170A (en) | Molten carbonate type fuel cell | |
| JP6917416B2 (en) | Electrochemical reaction cell stack | |
| JPH0697617B2 (en) | Molten carbonate fuel cell | |
| JP7237043B2 (en) | Electrochemical reaction cell stack | |
| JPS625569A (en) | Molten carbonate type fuel cell stack | |
| JPH1092447A (en) | Stacked fuel cell | |
| JP2021022460A (en) | Electrochemical reaction cell stack | |
| JP2004335179A (en) | Fuel cell | |
| JP7249981B2 (en) | Electrochemical reaction cell stack | |
| JP2554114B2 (en) | Fuel cell separator | |
| JP7757221B2 (en) | Complex | |
| JPH09283170A (en) | Flat solid oxide fuel cell | |
| JP7112443B2 (en) | Electrochemical reaction cell stack | |
| JP7186208B2 (en) | Electrochemical reaction cell stack | |
| JP2021140913A (en) | Manufacturing method of dummy electrode joint, fuel cell stack and dummy electrode joint | |
| JPH0665062B2 (en) | Fuel cell separator | |
| JP7611181B2 (en) | Complex | |
| JP7210509B2 (en) | Electrochemical reaction cell stack | |
| JP7507738B2 (en) | Electrochemical reaction unit and electrochemical reaction cell stack | |
| JP7522715B2 (en) | Electrochemical reaction cell stack | |
| JP3339720B2 (en) | Molten carbonate fuel cell | |
| JP7159126B2 (en) | Electrochemical reaction cell stack |