JPH0439868A - Separator for molten carbonate fuel cells - Google Patents
Separator for molten carbonate fuel cellsInfo
- Publication number
- JPH0439868A JPH0439868A JP2147616A JP14761690A JPH0439868A JP H0439868 A JPH0439868 A JP H0439868A JP 2147616 A JP2147616 A JP 2147616A JP 14761690 A JP14761690 A JP 14761690A JP H0439868 A JPH0439868 A JP H0439868A
- Authority
- JP
- Japan
- Prior art keywords
- current collector
- plate
- separator
- electrode
- contact
- 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
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 title claims description 22
- 239000000446 fuel Substances 0.000 title claims description 22
- 239000003792 electrolyte Substances 0.000 claims description 29
- 239000007789 gas Substances 0.000 claims description 15
- 239000002737 fuel gas Substances 0.000 claims description 7
- 230000001590 oxidative effect Effects 0.000 claims description 7
- 238000005192 partition Methods 0.000 claims description 4
- 238000005452 bending Methods 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 description 11
- 238000010586 diagram Methods 0.000 description 4
- 238000003825 pressing Methods 0.000 description 3
- 238000005520 cutting process Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000005489 elastic deformation Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000020169 heat generation Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000007665 sagging Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
Landscapes
- Fuel Cell (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は燃料の有する化学エネルギーを直接電気エネル
ギーに変換させるエネルギ一部門で用いる燃料電池のう
ち、特に、溶融炭酸塩型燃料電池に用いるセパレータに
関するものである。Detailed Description of the Invention [Field of Industrial Application] The present invention relates to a separator used in a molten carbonate fuel cell among fuel cells used in the energy sector that directly converts the chemical energy of fuel into electrical energy. It is related to.
[従来の技術]
従来の溶融炭酸塩型燃料電池は、第7図に一例の概略を
示す如く、電解質として溶融炭酸塩を多孔質物質にしみ
込ませてなる電解質板(タイル)1を、カソード(酸素
極)2とアノード(燃料極)3の両電極で両面から挟み
、カソード2側へ酸化ガスOGを供給すると共にアノー
ド3側へ燃料ガスFGを供給することによりカソード2
側とアノード3側で反応を行わせて、カソード2とアノ
ード3との間で発生する電位差により発電が行われるよ
うにしたものを1セルとし、各セルをセパレータ4を介
して多層に積層させてスタックとするようにしてある。[Prior Art] A conventional molten carbonate fuel cell, as shown schematically in FIG. The cathode 2 is sandwiched between both electrodes (oxygen electrode) 2 and anode (fuel electrode) 3, and oxidizing gas OG is supplied to the cathode 2 side, and fuel gas FG is supplied to the anode 3 side.
One cell is a cell in which a reaction is caused between the cathode 2 and the anode 3 side, and electricity is generated by the potential difference generated between the cathode 2 and anode 3, and each cell is laminated in multiple layers with a separator 4 in between. It is set up as a stack.
かかる溶融炭酸塩型燃料電池において用いられるセパレ
ータ4としては、センタープレート5の両面側にチャン
ネル形成部としてコルゲート板を配して3枚構造とし、
該コルゲート板をカレントコレクター6としたものが用
いられており、燃料電池セルを積層するときカソード2
とアノード3をカレントコレクター6により電解質板1
に押し当てるようにしている。The separator 4 used in such a molten carbonate fuel cell has a three-layer structure with corrugated plates arranged as channel forming portions on both sides of the center plate 5.
A corrugated plate is used as a current collector 6, and when stacking fuel cells, the cathode 2
and the anode 3 are connected to the electrolyte plate 1 by the current collector 6.
I try to press against it.
上記溶融炭酸塩型燃料電池のセルを構成する電解質板1
は、カソード2とアノード3の画電極側で反応するガス
同士を仕切る役割をすると共にカソード2側で生成され
る炭酸イオン(Co、= )をアノード3側へ通過させ
て電子を遮断する役割をしており、カソード2側へ酸化
ガスOGを供給すると、カレントコレクター6としての
コルゲート板で形成されたガス通路を酸化ガスが流れる
ことによって、カソード2側で、Co2+1/202+
2 e−−> CO3−の反応が行われて、炭酸イオ
ン(Co3= )が生じ、このCO3−が電解質板1中
を泳動しアノード3に到達する。一方、7ノード3側に
燃料ガスFGを供給すると、カレントコレクター6とし
てのコルゲート板で形成されたガス通路を燃料ガスが流
れる間にアノード3側で、
CO3−+)+2−)H20+CO2+2e−の、反応
が行われ、水素ガスが主として消費される。Electrolyte plate 1 constituting the cell of the molten carbonate fuel cell
plays the role of separating gases that react on the picture electrode side of the cathode 2 and anode 3, and also plays the role of allowing carbonate ions (Co, = ) generated on the cathode 2 side to pass to the anode 3 side and blocking electrons. When the oxidizing gas OG is supplied to the cathode 2 side, the oxidizing gas flows through the gas passage formed by the corrugated plate as the current collector 6, so that Co2+1/202+ is generated on the cathode 2 side.
The reaction 2e-->CO3- is performed to generate carbonate ions (Co3=), and this CO3- migrates through the electrolyte plate 1 and reaches the anode 3. On the other hand, when fuel gas FG is supplied to the 7 node 3 side, while the fuel gas flows through the gas passage formed by the corrugated plate as the current collector 6, on the anode 3 side, CO3-+)+2-)H20+CO2+2e-, A reaction takes place and hydrogen gas is primarily consumed.
したがって、燃料電池の性能を出すには、カソード2、
アノード3の各電極と電解質板1との当りが良くなけれ
ばならない。上記電極と電解質板1の当りの良し悪しは
、第7図の構成例の場合にはカレントコレクター6とし
てのコルゲート板とカソード2及びアノード3との当り
により決められるものであり、カレントコレクター6と
してのフルゲート板は、目標が±25虜という高い精度
が要求されているが、そこまで達していないのが現状で
ある。そのため、第8図に示す如く、カレントコレクタ
ー6としてのコルゲート板が部分的にカソード2又はア
ノード3に一様に当らないで、当っていない個所Aが生
じることがある。Therefore, in order to achieve the best performance of the fuel cell, the cathode 2,
The contact between each electrode of the anode 3 and the electrolyte plate 1 must be good. The quality of the contact between the electrode and the electrolyte plate 1 is determined by the contact between the corrugated plate as the current collector 6, the cathode 2, and the anode 3 in the case of the configuration example shown in FIG. The full-gate board requires high accuracy with a target of ±25 degrees, but at present it has not reached that level. Therefore, as shown in FIG. 8, the corrugated plate serving as the current collector 6 does not uniformly contact the cathode 2 or the anode 3 partially, and there may be a portion A where the corrugated plate does not contact the cathode 2 or the anode 3 uniformly.
[発明が解決しようとする課題]
ところが、上記した第8図の如く、カレントコレクター
6の電極への当りが一様でなくて、当りのない個所Aが
生じると、この個所へではカソード2又はアノード3と
電解質板1との当りか悪くなり、カソード2と電解質板
1との間では、カソード2側で生じた炭酸イオン(Go
、=)が電解質板1内へ流れにくくなる。すなわち、カ
ソード2と電解質板1とが離れているところでは炭酸イ
オン(C03= )の流れが妨げられるので、電池の内
部抵抗が大となるばかりでなく流れ易い個所での反応が
激しく進められることになって発熱が過大となり、炭酸
塩の消失に至る。又、アノード3と電解質板1との間で
も当りが悪いところがあると、電解質板1中を泳動する
炭酸イオン(Co3= )がアノード2に流れにくくな
る。[Problems to be Solved by the Invention] However, as shown in FIG. 8 above, if the contact of the current collector 6 with the electrode is not uniform and there is a portion A where no contact occurs, the cathode 2 or The contact between the anode 3 and the electrolyte plate 1 becomes poor, and between the cathode 2 and the electrolyte plate 1, carbonate ions (Go
, =) becomes difficult to flow into the electrolyte plate 1. In other words, the flow of carbonate ions (C03=) is impeded where the cathode 2 and electrolyte plate 1 are far apart, which not only increases the internal resistance of the battery, but also causes the reaction to proceed vigorously at locations where carbonate ions easily flow. This causes excessive heat generation, leading to the loss of carbonate. Furthermore, if there is poor contact between the anode 3 and the electrolyte plate 1, it becomes difficult for carbonate ions (Co3=) migrating in the electrolyte plate 1 to flow to the anode 2.
かかる問題をなくすためには、カレントコレクター6と
してのコルゲート板や、電極、電解質板の製作精度を高
める必要があるが、精度を高めるためには製作か大変で
あると共にコストアップが避けられない。In order to eliminate this problem, it is necessary to improve the manufacturing accuracy of the corrugated plate as the current collector 6, the electrodes, and the electrolyte plate, but increasing the accuracy requires difficult manufacturing and inevitably increases costs.
又、燃料電池は、長時間高温運転をしていると、部品の
クリープにより、第9図に概略を示す如く、カソード2
、アノード3の電極表面が変形して来ると、カレントコ
レクター6とカソード2、アノード3との当りのない個
所8が生じて来てカソード2、アノード3と電解質板1
との当りが時間とともに悪くなって来るが、従来のカレ
ントコレクター6は、コルゲート板で、その1山の曲り
部を見ると、第10図に示す両端支持の剛構造でフレキ
シブルでないため、弾性が少なく、上記クリープによる
変形により電極と電解質板1との当りが悪くなって来て
も、カレントコレクター6がその変形に追従できず、又
、歪が大きく平坦な製品ができず、製作時に生じた寸法
誤差に基づく不均一な当りの吸収は勿論のこと、クリー
プ量の吸収をすることができない。In addition, when a fuel cell is operated at high temperatures for a long period of time, the cathode 2 is damaged due to creep of parts, as shown schematically in FIG.
When the electrode surface of the anode 3 is deformed, areas 8 where the current collector 6, cathode 2, and anode 3 do not touch are generated, and the cathode 2, anode 3, and electrolyte plate 1
However, the conventional current collector 6 is made of a corrugated board, and if you look at the curved part of one peak, as shown in Fig. 10, it has a rigid structure with support at both ends and is not flexible, so it has low elasticity. Even if the contact between the electrode and the electrolyte plate 1 becomes poor due to the deformation caused by the above-mentioned creep, the current collector 6 cannot follow the deformation, and it is difficult to produce a flat product with large distortions, which may occur during manufacturing. Not only can it absorb uneven hits due to dimensional errors, but it also cannot absorb the amount of creep.
更に、従来のカレントコレクター6としてのコルゲート
板は、表面積が大きいので、ぬれ面積が大となり、炭酸
塩のロスが大きい。Furthermore, since the corrugated plate used as the conventional current collector 6 has a large surface area, the wetted area is large and the loss of carbonate is large.
そこで、本発明は、カレントコレクター、電極、電解質
板を精度良く作らなくても各部で一様な当りが得られる
ようにすると共にクリープによる変形にも容易に追従し
て常に良好な当りが得られるようにし、更に簡単に製作
できるような溶融炭酸塩型燃料電池用セパレータを提供
しようとするものである。Therefore, the present invention makes it possible to obtain uniform contact at each part even if the current collector, electrode, and electrolyte plate are not made with high precision, and also easily follows deformation due to creep, thereby making it possible to always obtain good contact. The present invention aims to provide a separator for a molten carbonate fuel cell that can be manufactured more easily.
[課題を解決するための手段]
本発明は、上記課題を解決するために、電解質板をカソ
ードとアノードの両電極で両面から挟んでカソード側に
酸化ガスを供給すると共にアノード側に燃料ガスを供給
するようにしてあるセルを多層に積層するときの仕切り
として用いる溶融炭酸塩型燃料電池用セパレータにおい
て、センタープレートとカソードとの間及びセンタープ
レートとアノードとの間にガス通路を形成するためにセ
ンタープレートの両側に配置されるカレントコレクター
を、プレートに多数の矩形の開口部を形成すると共に各
開口部に1つの押切り片を片持支持構造で折曲げ加工し
てなる構造とし、且つ上記開口部は開口率を30%〜6
0%とすると共に開口部の狭い方の幅寸法を2Nn〜6
mとした構成とする。又、上記押切り片は先端を湾曲さ
せて湾曲部がセンタープレートに当接するようにすると
よい。[Means for Solving the Problems] In order to solve the above problems, the present invention provides an electrolyte plate that is sandwiched between both electrodes, a cathode and an anode, to supply oxidizing gas to the cathode side and supply fuel gas to the anode side. In a separator for a molten carbonate fuel cell, which is used as a partition when stacking cells in a multi-layered manner, for forming gas passages between the center plate and the cathode and between the center plate and the anode. The current collectors disposed on both sides of the center plate have a structure in which a large number of rectangular openings are formed in the plate and one pressed piece is bent in each opening with a cantilever support structure, and The aperture ratio is 30% to 6.
0% and the narrower width of the opening is 2Nn~6
The configuration is set to m. Moreover, it is preferable that the tip of the press-cut piece is curved so that the curved part contacts the center plate.
[作 用]
カレントコレクターを構成するプレートの開口率が30
%〜60%としであるので、電極へのガスの拡散が良好
に行われると共に電極の支持も充分に行われる。又、各
開口部の狭い方の寸法を2#1〜6Mとすると、開口部
の形成と押切り片の折り曲げを行うプレスの金型の摩耗
を少なくできる上に、電極の支持に支障をきたすことも
ない。センタープレート側に折り曲げた押切り片は、片
持ち式でフレキシビリティがあり、カレントコレクター
自体、あるいは電極、電解質板に製作誤差かあっても、
又、クリープが生じても、カレントコレクターの弾性に
よりカレントコレクターは電極に一様に当って電極と電
解質板とを全面にわたり均一に接触させることができる
。又、カレントコレクターは、プレスによる一工程で成
形できるので、製作か容易である。又、カレントコレク
ターとしての押切り片の先端を湾曲させるようにプレス
で押切り成形すると、先端の高さが均一となり、高さ精
度を良好にできることになる。[Function] The aperture ratio of the plate constituting the current collector is 30.
% to 60%, gas is well diffused into the electrode and the electrode is sufficiently supported. In addition, if the narrower dimension of each opening is set to 2#1 to 6M, it is possible to reduce the wear of the press die that forms the opening and bends the pressed piece, and also prevents the support of the electrode from becoming a problem. Not at all. The pressed piece bent toward the center plate is cantilevered and flexible, so even if there are manufacturing errors in the current collector itself, electrodes, or electrolyte plate,
Furthermore, even if creep occurs, the elasticity of the current collector makes it possible for the current collector to uniformly contact the electrode and bring the electrode and electrolyte plate into uniform contact over the entire surface. In addition, the current collector is easy to manufacture because it can be molded in one step using a press. Further, if the tip of the pressed piece serving as the current collector is press-cut so as to be curved, the height of the tip becomes uniform, and the height accuracy can be improved.
[実 施 例] 以下、本発明の実施例を図面を参照して説明する。[Example] Embodiments of the present invention will be described below with reference to the drawings.
第1図乃至第3図は本発明の一実施例を示すもので、電
解質板1をカソード2とアノード3の両電極で両面から
挟んで、カソード2側へ酸化ガスOGを供給すると共に
アノード3側に燃料ガスFGを供給するようにしてある
セルを多層に積層するときの仕切板として用いる溶融炭
酸塩型燃料電池用セパレータにおいて、本発明のセパレ
ータ7は、センタープレート8と、該センタープレート
8の両側にあってセンタープレート8とカソード2との
間及びセンタープレート8とアノード3との間にそれそ
゛れガス通路を形成すると共にカソード2とアノード3
を支持する機能を有するカレントコレクター9とからな
る構成とし、全体としてカソード2側の酸化ガスOGと
アノード3側の燃料ガスFGを仕切るようにしである。1 to 3 show an embodiment of the present invention, in which an electrolyte plate 1 is sandwiched between both electrodes, a cathode 2 and an anode 3, and oxidizing gas OG is supplied to the cathode 2 side, while the anode 3 In a separator for a molten carbonate fuel cell, which is used as a partition plate when stacking cells in multiple layers to supply fuel gas FG to the side thereof, the separator 7 of the present invention includes a center plate 8 and a center plate 8. gas passages are formed between the center plate 8 and the cathode 2 and between the center plate 8 and the anode 3, and between the cathode 2 and the anode 3.
The current collector 9 has a function of supporting the current collector 9, and the oxidizing gas OG on the cathode 2 side and the fuel gas FG on the anode 3 side are separated as a whole.
上記カレントコレクター9は、第4図に示す如き作用面
を傾斜させてなるプレス金型10によりプレート9aに
多数の開口部9bを押切り形成するとき、同時に開口部
9bの一部より延長する押切り片9Cを折り曲げ加工し
てプレート9aの片面側に突出させた構成とし、゛且つ
上記各開口部9bを形成するときの開口率を30%〜6
0%位とし、更に開口部の寸法として、狭い方の幅寸法
eを2mm〜6mとする。When the current collector 9 is pressed to form a large number of openings 9b in the plate 9a using a press die 10 having an inclined working surface as shown in FIG. The cut piece 9C is bent to protrude from one side of the plate 9a, and the aperture ratio when forming each of the openings 9b is 30% to 6.
0%, and the narrower width e of the opening is 2 mm to 6 m.
上記開口率を30%〜60%とするのは、30%以下で
は、孔か少なくて電極へのガスの流配、拡散か悪くなり
、60%以上では孔が多すぎて電極を電解質板1に強く
押し付けられなくて電極が垂れて来ることがあり、電極
支持板として機能し得なくなるからである。又、開口部
9bの狭い方の幅寸法を2#!!!1〜61Mtとする
のは、2m以下の場合はプレス成形するときにプレス金
型の摩耗が激しく、金型が摩耗すると、切り口にバリが
出て来る問題があり、64!I11以上では電極の支持
か不充分となって電極が垂れて来る問題がおるからであ
る。The above-mentioned aperture ratio is set to 30% to 60% because if it is less than 30%, there will be fewer holes and gas distribution and diffusion to the electrode will be poor, and if it is more than 60%, there will be too many holes and the electrode will not be connected to the electrolyte plate. This is because the electrodes may sag if they are not pressed firmly against the electrodes, making it impossible to function as an electrode support plate. Also, the width of the narrower side of the opening 9b is 2#! ! ! The reason why it is set at 1 to 61 Mt is because if it is less than 2 m, the press mold will be severely worn during press forming, and when the mold wears, there will be a problem that burrs will appear on the cut end. This is because if the electrode is more than I11, the electrode will not be supported sufficiently and there will be a problem that the electrode will sag.
第4図に示す如きプレス金型10を用いてカレントコレ
クター9を成形する場合、第5図に示す如くプレート9
aの開口部9bをプレス金型10で押切りするとき、切
り口は引き裂かれるようになるので、バリ11が生じる
が、矢印aの方向からプレス金型10により押切られる
ため、押切り片9Cの先端のバリ11は内側に生じるこ
とになる。When molding the current collector 9 using the press mold 10 as shown in FIG. 4, the plate 9 as shown in FIG.
When the opening 9b of a is pressed with the press die 10, the cut end is torn and a burr 11 is generated. The burr 11 at the tip will be formed on the inside.
この場合、バリ11が押切り片9Cの先端の外側に形成
されると、このバリ11がセンタープレート8に接する
ことになってカレントコレクタ−9自体の高さ調整がで
きないと共に、バリ11か変形するので高さの精度が出
せないということになるが、本発明では、バリ11は押
切り片9Cの先端の内側に出来るので、上記の問題はな
い。In this case, if the burr 11 is formed on the outside of the tip of the pressed piece 9C, the burr 11 comes into contact with the center plate 8, making it impossible to adjust the height of the current collector 9 itself, and the burr 11 deforms. Therefore, height accuracy cannot be achieved, but in the present invention, the burr 11 is formed inside the tip of the press-off piece 9C, so the above problem does not occur.
本発明では、1枚のプレート9aに対して第4図の如き
プレス金型10を多数セットして、−度にプレス金型1
0を作動させて押切り成形するので、−工程で多数の開
口部9bの形成と押切り片9Cの折曲げ加工を行うこと
ができて、カレントコレクター9の製作を容易に行うこ
とができる。In the present invention, a large number of press molds 10 as shown in FIG. 4 are set for one plate 9a, and each press mold 10 is
Since the extrusion molding is performed by operating the 0, the formation of a large number of openings 9b and the bending of the extrusion pieces 9C can be performed in the - step, making it possible to easily manufacture the current collector 9.
上述のように製作した本発明のセパレータ7は、カレン
トコレクター9が各開口部9bごとに片持ち式で7レキ
シビリテイになっているので、たとえば、第1図及び第
3図に示す如く押切り片9Cをセンタープレート8に当
接するようにセットした構成とし、セルの仕切板として
用いて積層方向に締付力を与えた場合は、カレントコレ
クター9の押切り片9Cの先端がセンタープレート8に
沿い摺動しながら弾性により矢印す方向へ逃げることが
できて容易に変形できる。又、所定の締付力が付与させ
である状態において、電極のクリープ等のために電極と
センタープレート8との間の間隔が広がるような変化が
生じたときは、該当個所のセンタープレート8に接して
いる押切り片9Cの先端かセンタープレート8に沿い摺
動しながら弾性により矢印C方向へ移行して起立して来
るように変形できる。したがって、第8図に示す従来方
式の如く、カレントコレクター6の寸法精度に誤差があ
って、カレントコレクター6が部分的に電極に当らない
ところが生じるような場合、従来の方式では、締付力を
付与させても、カレントコレクター6は曲り部が両側支
持構造で剛性が高く弾性が少ないものであったため、電
極に当らない部分はそのまま残っていたが、本発明では
、上述のように締付力を付与させると、押切り片9Cの
センタープレート8との接触部が弾性により変形できる
ことから、既に電極に当っている部分のセンタープレー
トとの接触部は、未だ電極に当っていない個所のカレン
トコレクター9が電極に当るまで変形を続けるので、カ
レントコレクター9の製作時の寸法誤差が市っても、そ
の誤差を吸収させることができる。電極や電解質板1の
製作精度が悪くて電極と電解質板1との当りの悪いとこ
ろが生じる場合でも、同様にカレントコレクター9の押
切り片9Cの弾性による変形により一様な当りにするこ
とができる。又、燃料電池を長時間高温運転することに
より、たとえば、カソード2やアノード3の電極のクリ
ープ量か多く、当該部分へのカレントコレクター9の当
りが弱くなって来て電極と電解質板との当りか時間とと
もに悪くなるような事態が生じた場合でも、本発明では
、カレントコレクター9の押切り片9cが片持支持構造
で弾性を有しているため、上記のクリープ量を吸収して
電極と電解質板1との全面にわたり一様な当りが得られ
るようにすることができる。In the separator 7 of the present invention manufactured as described above, the current collector 9 is cantilevered at each opening 9b and has 7 flexibilities. 9C is set so as to be in contact with the center plate 8, and when it is used as a cell partition plate and a tightening force is applied in the stacking direction, the tip of the press-cut piece 9C of the current collector 9 aligns with the center plate 8. While sliding, it can escape in the direction of the arrow due to its elasticity and can be easily deformed. In addition, when a change occurs in which the gap between the electrode and the center plate 8 widens due to creep of the electrode while the predetermined tightening force is being applied, the center plate 8 at the corresponding location is While sliding along the center plate 8, the tip of the pressing piece 9C that is in contact with it can be elastically deformed so as to move in the direction of arrow C and rise up. Therefore, when there is an error in the dimensional accuracy of the current collector 6, as in the conventional method shown in FIG. Even if the current collector 6 was applied with the clamping force as described above, the bent portion of the current collector 6 had a structure with both sides supported and had high rigidity and low elasticity, so the portion that did not contact the electrode remained as it was. When this is applied, the contact part of the push-cut piece 9C with the center plate 8 can be elastically deformed, so that the contact part with the center plate of the part that is already in contact with the electrode becomes the current collector of the part that is not in contact with the electrode yet. Since the deformation continues until the current collector 9 hits the electrode, even if there is a dimensional error in manufacturing the current collector 9, that error can be absorbed. Even if the manufacturing precision of the electrodes and electrolyte plate 1 is poor, resulting in poor contact between the electrode and electrolyte plate 1, uniform contact can be achieved by elastic deformation of the press-cut pieces 9C of the current collector 9. . In addition, when a fuel cell is operated at high temperatures for a long period of time, for example, the amount of creep in the cathode 2 and anode 3 electrodes increases, and the contact of the current collector 9 with these parts becomes weaker, causing contact between the electrodes and the electrolyte plate. Even if a situation that worsens over time occurs, in the present invention, the push piece 9c of the current collector 9 has a cantilever support structure and has elasticity, so it absorbs the amount of creep and remains connected to the electrode. Uniform contact with the electrolyte plate 1 can be obtained over the entire surface.
次に、第6図は本発明の他の例を示すもので、押切り片
9Cの先端部を湾曲するように折曲げ加工し、該押切り
片9Cの先端湾曲面をセンタープレート8に当接させる
ようにしたものである。Next, FIG. 6 shows another example of the present invention, in which the tip of the press-cut piece 9C is bent so as to be curved, and the curved tip of the press-cut piece 9C is brought into contact with the center plate 8. It was designed so that they were in contact with each other.
この例によれば、押切り片9Cの長さ如何にかかわらず
、押切り片9Cの先端部の湾曲面がセンタープレート8
に接することになり、押切り片9Cの先端のカット面が
センタープレート8に接することがないことから、カレ
ントコレクター9の高さ精度を良好なものとすることが
できる。According to this example, regardless of the length of the press-cut piece 9C, the curved surface of the tip of the press-cut piece 9C is
Since the cut surface at the tip of the pressed cut piece 9C does not come into contact with the center plate 8, the height accuracy of the current collector 9 can be made good.
なお、上記実施例では、開口部9bを矩形状として広い
幅の一部に押切り片9cを延長させた場合を示したが、
幅の狭い方の一部に押切り片9Cが延長するようなプレ
ス金型を用いて成形するようにしてもよく、又、各開口
部9bの押切り片9Cの延長方向を同一方向とした場合
を示したが、隣接する開口部9b間で押切り片9Cの延
長方向が互に向い合うような方向となるようにじてもよ
い。In addition, in the above embodiment, the case where the opening 9b is rectangular and the push-cut piece 9c is extended to a part of the wide width is shown.
The molding may be performed using a press mold in which the pressed piece 9C extends to a part of the narrow side, and the extending direction of the pressed piece 9C of each opening 9b is the same direction. Although the case is shown, the extension directions of the push-cut pieces 9C may be arranged to face each other between the adjacent openings 9b.
[発明の効果]
以上述べた如く、本発明の溶融炭酸塩型燃料電池用セパ
レータによれば、プレートに多数の開口部をプレス金型
により押切り形成して、各開口部ごとに1片の押切り片
を片側へ折り曲げて突出させ、且つ上記開口部の開口率
を30%〜60%の範囲にすると共に各開口部の狭い方
の幅寸法を2IMt〜6Al11にした構成のカレント
コレクターを、センタープレートの両面側に配してなる
構成としであるので、次の如き優れた効果を奏し得る。[Effects of the Invention] As described above, according to the molten carbonate fuel cell separator of the present invention, a large number of openings are formed in the plate using a press die, and one piece is formed for each opening. A current collector having a structure in which a pressed piece is bent to one side to protrude, the aperture ratio of the opening is in the range of 30% to 60%, and the width of the narrower side of each opening is 2IMt to 6Al11, Since it is arranged on both sides of the center plate, the following excellent effects can be achieved.
(1) カレントコレクターの開口率を30%〜60
%にしているので、電極へのガスの拡散が良好に行われ
ると共に電極の支持も充分に行え、又、開口の狭い方の
寸法を2#1〜6#EI11としているので、プレス金
型で開口を形成する際にプレス金型の摩耗を低減できる
と同時に電極支持において電極が垂れて来るのを防止で
きる。(1) Increase the aperture ratio of the current collector from 30% to 60
%, the gas can diffuse well into the electrode, and the electrode can be supported sufficiently. Also, since the narrower dimension of the opening is 2#1 to 6#EI11, it can be easily used in press molds. It is possible to reduce wear on the press die when forming the opening, and at the same time prevent the electrode from sagging when supporting the electrode.
(it) 1つの開口部に1つの押切り片を折曲げ加
工して片持支持構造としであるので、カレントコレクタ
ーは弾性を有していて、カレントコレクター、電極、電
解質板の製作精度が悪くて寸法精度に誤差があっても、
燃料電池として組み立てて所定の締付力を付与させたと
きに上記誤差を吸収させて−様な当りが得られるように
でき、カレントコレクター、電極、電解質板の製作精度
を高める必要がなく製作が楽であると共に、安価に製作
できることになる。(IT) Since one pressed piece is bent into one opening to form a cantilever support structure, the current collector has elasticity, and the manufacturing accuracy of the current collector, electrode, and electrolyte plate is poor. Even if there is an error in dimensional accuracy,
When assembled as a fuel cell and applying a predetermined tightening force, it is possible to absorb the above error and obtain a similar hit, and there is no need to improve the manufacturing precision of the current collector, electrode, and electrolyte plate, making the manufacturing process easier. It is easy and can be manufactured at low cost.
(lli) 運転中において部品のクリープによる変
形が生じても、カレントコレクターの弾性によりその変
形に追従してクリープ量を吸収することができ、クリー
プにより電極と電解質板との当りが悪くなって来る事態
が避けられる。(lli) Even if parts are deformed due to creep during operation, the elasticity of the current collector can follow the deformation and absorb the amount of creep, and the contact between the electrode and the electrolyte plate becomes worse due to creep. The situation can be avoided.
(転)従来のカレントコレクターの如きコルゲート板の
1山の曲り部を両端支持の剛構造としたものを、弾性を
もたせるために上記1山の曲り部の中央部を切断して片
持支持構造に成形することもできる。しかし、この形式
のものではプレス工程と切断工程の2工程が必要である
と共に、中央部を切断して片持支持にするとき、カッタ
ーの刃が切れなくなって来ると切断部のパリが外側に出
張って来てカレントコレクターの^さ精度が悪くなるが
、本発明では1つの開口部に1つの押切り片を片持支持
で成形させるようにしであるので、プレス金型によるプ
レス工程のみてよく、より簡易に製作できると共に、切
り口にパリか出てもそのパリは内側に出るので、高さ精
度を悪くすることかない。(Translation) A conventional current collector has a rigid structure in which a single curved part of a corrugated board is supported at both ends, but the central part of the single curved part is cut to provide elasticity, resulting in a cantilever support structure. It can also be formed into However, this type of product requires two steps, a pressing process and a cutting process, and when cutting the center part and making it cantilever supported, when the cutter blade becomes hard to cut, the edge of the cut part will move outward. The precision of the current collector deteriorates when the current collector is moved out, but in the present invention, one pressed piece is molded in one opening with cantilever support, so the pressing process using a press mold is sufficient. , it can be manufactured more easily, and even if there is a burr at the cut end, the burr will come out on the inside, so the height accuracy will not be degraded.
(V) 各開口部の押切り片の先端部を湾曲させて、
湾曲部の外側をセンタープレートあるいは電極に接触さ
せるようにすることにより、押切り片の先端か不揃いで
あったとしてもカレントコレクターの高さは均一にでき
て、高さ精度をより良好にできる。(V) Curving the tip of the pressed piece of each opening,
By bringing the outside of the curved portion into contact with the center plate or electrode, the height of the current collector can be made uniform even if the tips of the pressed pieces are uneven, and the height accuracy can be improved.
第1図は本発明のセパレータを用いた溶融炭酸塩型燃料
電池の一部の断面図、第2図は本発明のセパレータにお
けるカレントコレクターの一例を示す斜視図、第3図は
第1図の■部の拡大図、第4図は本発明のセパレータに
おけるカレントコレクターの成形に用いるプレス金型の
概略図、第5図はプレス金型で開口部及び押切り片を押
切り成形するときに生じるパリを示す図、第6図は本発
明のセパレータの伯の例を示すカレントコレクターの断
面図、第7図は従来の溶融炭酸塩型燃料電池の一例を示
す一部の断面図、第8図はカレントコレクターと電極と
が当っていないところの状態を示す断面図、第9図は電
極がクリープで変形してカレントコレクターの当らない
個所が生じた状態を示す概略図、第10図は従来のカレ
ントコレクターの構造を示す図である。
1・・・電解質板、2・・・カソード、3・・・アノー
ド、4.7・・・セパレータ、8・・・センタープレー
ト、9・・・カレントコレクター、9a・・・プレート
、9b・・・開口部、9C・・・押切り片、10・・・
プレス金型。・第2図FIG. 1 is a cross-sectional view of a part of a molten carbonate fuel cell using the separator of the present invention, FIG. 2 is a perspective view showing an example of a current collector in the separator of the present invention, and FIG. 3 is the same as that of FIG. Fig. 4 is a schematic diagram of the press mold used for forming the current collector in the separator of the present invention, Fig. 5 is an enlarged view of part ①, and Fig. 5 is a schematic diagram of the press mold used to form the current collector in the separator of the present invention. 6 is a sectional view of a current collector showing an example of the separator of the present invention, FIG. 7 is a partial sectional view showing an example of a conventional molten carbonate fuel cell, and FIG. 8 9 is a cross-sectional view showing a state where the current collector and electrode do not touch each other, FIG. 9 is a schematic diagram showing a state where the electrode is deformed due to creep and there are places where the current collector does not touch, and FIG. 10 is a conventional FIG. 3 is a diagram showing the structure of a current collector. DESCRIPTION OF SYMBOLS 1... Electrolyte plate, 2... Cathode, 3... Anode, 4.7... Separator, 8... Center plate, 9... Current collector, 9a... Plate, 9b...・Opening part, 9C... Press cut piece, 10...
Press mold.・Figure 2
Claims (2)
ら挟んでカソード側に酸化ガスを供給すると共にアノー
ド側に燃料ガスを供給するようにしてあるセルを多層に
積層するときの仕切板として用いる溶融炭酸塩型燃料電
池用セパレータにおいて、プレートに矩形の開口部を多
数設けて、該各開口部に1つの押切り片を片持ち式に折
曲げ成形してなり且つ上記開口部の開口率を30%〜6
0%とすると共に開口部の狭い方の幅寸法を2mm〜6
mmとしてあるカレントコレクターを、センタープレー
トの両面に接して配置してなることを特徴とする溶融炭
酸塩型燃料電池用セパレータ。(1) An electrolyte plate is sandwiched between the cathode and anode electrodes to supply oxidizing gas to the cathode side and fuel gas to the anode side. Used as a partition plate when stacking cells in multiple layers. In a separator for a molten carbonate fuel cell, a plate is provided with a large number of rectangular openings, each opening is formed by bending one pressed piece in a cantilevered manner, and the aperture ratio of the openings is 30%~6
0% and the narrower width of the opening is 2mm to 6mm.
1. A separator for a molten carbonate fuel cell, characterized in that current collectors having a diameter of 1 mm are arranged in contact with both sides of a center plate.
湾曲させて湾曲部の外側をセンタープレートに接触させ
るように配してなる請求項(1)記載の溶融炭酸塩型燃
料電池用セパレータ。(2) The separator for a molten carbonate fuel cell according to claim (1), wherein the tip of the press-cut piece of the current collector is curved inward so that the outside of the curved portion is in contact with the center plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2147616A JPH0439868A (en) | 1990-06-06 | 1990-06-06 | Separator for molten carbonate fuel cells |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2147616A JPH0439868A (en) | 1990-06-06 | 1990-06-06 | Separator for molten carbonate fuel cells |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0439868A true JPH0439868A (en) | 1992-02-10 |
Family
ID=15434355
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2147616A Pending JPH0439868A (en) | 1990-06-06 | 1990-06-06 | Separator for molten carbonate fuel cells |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0439868A (en) |
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|---|---|---|---|---|
| KR100491688B1 (en) * | 1996-10-30 | 2005-08-24 | 술저 헥시스 악티엔게젤샤프트 | Flat High Temperature Fuel Cell Battery |
| JP2006512743A (en) * | 2002-12-24 | 2006-04-13 | フュエルセル エナジー, インコーポレイテッド | Inert end cell assembly for improved electrolyte management and electrical contact for fuel cells |
| JP2007323893A (en) * | 2006-05-31 | 2007-12-13 | Toyota Motor Corp | Fuel cell and manufacturing method thereof |
| JP2012129108A (en) * | 2010-12-16 | 2012-07-05 | Nissan Motor Co Ltd | Fuel cell stack |
| JP2013097982A (en) * | 2011-10-31 | 2013-05-20 | Nissan Motor Co Ltd | Fuel cell stack |
| JP2013229159A (en) * | 2012-04-25 | 2013-11-07 | Nissan Motor Co Ltd | Fuel cell stack |
| JP2016149244A (en) * | 2015-02-12 | 2016-08-18 | 本田技研工業株式会社 | Power storage module |
| KR20210110595A (en) * | 2018-11-30 | 2021-09-08 | 엑손모빌 리서치 앤드 엔지니어링 컴퍼니 | Cathode collector structure for molten carbonate fuel cell |
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| US11476486B2 (en) | 2018-11-30 | 2022-10-18 | ExxonMobil Technology and Engineering Company | Fuel cell staging for molten carbonate fuel cells |
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1990
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|---|---|---|---|---|
| KR100491688B1 (en) * | 1996-10-30 | 2005-08-24 | 술저 헥시스 악티엔게젤샤프트 | Flat High Temperature Fuel Cell Battery |
| JP2006512743A (en) * | 2002-12-24 | 2006-04-13 | フュエルセル エナジー, インコーポレイテッド | Inert end cell assembly for improved electrolyte management and electrical contact for fuel cells |
| JP2007323893A (en) * | 2006-05-31 | 2007-12-13 | Toyota Motor Corp | Fuel cell and manufacturing method thereof |
| JP2012129108A (en) * | 2010-12-16 | 2012-07-05 | Nissan Motor Co Ltd | Fuel cell stack |
| JP2013097982A (en) * | 2011-10-31 | 2013-05-20 | Nissan Motor Co Ltd | Fuel cell stack |
| JP2013229159A (en) * | 2012-04-25 | 2013-11-07 | Nissan Motor Co Ltd | Fuel cell stack |
| JP2016149244A (en) * | 2015-02-12 | 2016-08-18 | 本田技研工業株式会社 | Power storage module |
| US11616248B2 (en) | 2018-11-30 | 2023-03-28 | ExxonMobil Technology and Engineering Company | Elevated pressure operation of molten carbonate fuel cells with enhanced CO2 utilization |
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