JPH07161366A - Separator for fuel cell - Google Patents

Separator for fuel cell

Info

Publication number
JPH07161366A
JPH07161366A JP5339863A JP33986393A JPH07161366A JP H07161366 A JPH07161366 A JP H07161366A JP 5339863 A JP5339863 A JP 5339863A JP 33986393 A JP33986393 A JP 33986393A JP H07161366 A JPH07161366 A JP H07161366A
Authority
JP
Japan
Prior art keywords
gas flow
gas
center plate
flow path
anode
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.)
Granted
Application number
JP5339863A
Other languages
Japanese (ja)
Other versions
JP3265782B2 (en
Inventor
Naoki Fujiwara
直樹 藤原
Nobuyuki Arima
信之 在間
Mitsuo Otsubo
三生 大坪
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
IHI Corp
Original Assignee
IHI Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by IHI Corp filed Critical IHI Corp
Priority to JP33986393A priority Critical patent/JP3265782B2/en
Publication of JPH07161366A publication Critical patent/JPH07161366A/en
Application granted granted Critical
Publication of JP3265782B2 publication Critical patent/JP3265782B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/02Details
    • H01M8/0202Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/0247Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the form
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/02Details
    • H01M8/0202Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/0258Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/24Grouping of fuel cells, e.g. stacking of fuel cells
    • H01M8/2465Details of groupings of fuel cells
    • H01M8/2483Details of groupings of fuel cells characterised by internal manifolds
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel 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)

Abstract

PURPOSE:To control the pressure difference between electrodes and improve the flow rate distributing function by keeping balance between pressure loses of a fuel gas supplied to the anode side and an oxidizing gas supplied to the cathode side. CONSTITUTION:Gas flow routes in the cathode side and gas flow routes in the anode side are formed in the front and the rear sides of the center part of the center plate 9 except the peripheral parts by press-processing. Manifold 7 to send an oxidizing gas to the gas flow routes to the cathode side and manifold 7 to send a fuel gas to the gas flow routes in the anode side are formed in the peripheral parts of the center plate 9. Small projected parts 19 are formed in the gas flow route faces 12a which are communicated with the gas flow routes in the cathode side in the peripheral parts of the center plate 9 and projected parts 20 with wide width are formed in the gas flow route faces which are communicated with the gas flow routes in the anode side. The flow of the fuel gas is regulated by the projected parts 20 with wide width.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【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ー部門
で用いる燃料電池においてセルを仕切るために用いる燃
料電池用セパレータに関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a fuel cell separator used for partitioning cells in a fuel cell used in the energy sector for directly converting chemical energy of fuel into electric energy.

【0002】[0002]

【従来の技術】燃料電池のうち、溶融炭酸塩型燃料電池
は、図3に一例を示す如く、電解質として溶融炭酸塩を
多孔質物質にしみ込ませたタイル(電解質板)1をカソ
ード(酸素極)2とアノード(燃料極)3の両電極で挟
み、カソード2側に酸化ガスOGを供給すると共にアノ
ード3側に燃料ガスFGを供給することによりカソード
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4とし、各セル4をセパ
レータ5を介し多層に積層させてスタックとするように
してある。
2. Description of the Related Art Among fuel cells, a molten carbonate fuel cell has a tile (electrolyte plate) 1 in which a molten carbonate as an electrolyte is impregnated in a porous material as a cathode (oxygen electrode), as shown in FIG. ) 2 and an anode (fuel electrode) 3 sandwiched between them, and a potential difference generated between the cathode 2 and the anode 3 by supplying the oxidizing gas OG to the cathode 2 side and the fuel gas FG to the anode 3 side. One cell 4 is configured to generate power by means of the above, and each cell 4 is laminated in multiple layers via a separator 5 to form a stack.

【0003】上記燃料電池のセル4を積層するときの仕
切りとなる上記セパレータ5は、内部マニホールド型の
燃料電池にあっては周辺部を除く中央部分にガス流路と
なる凹凸を表裏両面に形成し、周辺部には酸化ガスOG
の給排用のマニホールド6と燃料ガスFGの給排用のマ
ニホールド7が設けてあって、ウェットシール部として
あり、上記セパレータ5の表裏両面を異なるガスが流れ
るように各ガスの給排用のマニホールドと中央部分のガ
ス流路とを連通させた構成としてある。8は中央部分を
切り抜いてセパレータ5の周辺部に配したディスタンス
ピースである。
The separator 5, which serves as a partition when the cells 4 of the fuel cell are stacked, has an unevenness serving as a gas flow path on the front and back sides in the central portion excluding the peripheral portion in the internal manifold type fuel cell. Oxidizing gas OG in the surrounding area
A manifold 6 for supplying / discharging the fuel gas FG and a manifold 7 for supplying / discharging the fuel gas FG are provided as a wet seal portion, and are used for supplying / discharging each gas so that different gases flow on both front and back surfaces of the separator 5. The configuration is such that the manifold and the gas passage in the central portion are communicated with each other. Reference numeral 8 is a distance piece cut out in the central portion and arranged in the peripheral portion of the separator 5.

【0004】又、上記セパレータ5としては、中央部分
のガス流路形成用の凹凸部をエッチング、機械掘加工、
プレス等により成形させる型式のもの、あるいは、セン
タープレートの両面側にコルゲート板を配してコルゲー
ト板によりガス流路を形成させるようにしたプレス型式
のもの等がある。
Further, as the separator 5, the uneven portion for forming the gas flow path in the central portion is etched, machined,
There is a type that is molded by a press or the like, or a press type that has corrugated plates arranged on both sides of the center plate to form a gas flow path by the corrugated plates.

【0005】上記プレス型式のセパレータ5であって内
部マニホールド型のものにあっては、図4及び図5に一
例を示す如く、センタープレート9の周辺部を除く中央
部分の表裏に、カソード側ガス流路12とアノード側ガ
ス流路13が形成されるようにしたガス流路形成用凹凸
部10をプレス成形により設け、更に、該センタープレ
ート9の周辺部の表裏面側に、中央部分を切り抜き且つ
周辺のタイル1よりも大きい寸法としたマスク板14,
15をそれぞれ配置し、該マスク板14,15の各周辺
部を屈曲させてセンタープレート9に重ね合わせ、重合
部を固着してシールさせるようにし、酸化ガス給排用の
マニホールド6を通して上記カソード側ガス流路12に
酸化ガスを、又、燃料ガス給排用のマニホールド7を通
して上記アノード側ガス流路13に燃料ガスをそれぞれ
送給するようにし、更に、上記センタープレート9のマ
ニホールド6,7が設けられている周辺部の表裏両面
に、同じ形状のエンボス加工により形成した小突起1
7,18を所要間隔で配列し、該小突起17,18によ
ってマスク板14,15とセンタープレート9との間の
間隔が一定に保持されるようにすると共に、上記ガス流
路12,13へ流すガスを分散させられるようにしてあ
る。11はスペーサブロックを示す。
In the case of the press type separator 5 which is an internal manifold type, as shown in FIGS. 4 and 5, one example is shown in FIGS. A gas flow path forming concavo-convex portion 10 in which a flow path 12 and an anode gas flow path 13 are formed is provided by press molding, and a central portion is cut out on the front and back sides of the peripheral portion of the center plate 9. Moreover, the mask plate 14 having a size larger than the surrounding tiles 1,
15 are arranged respectively, the peripheral portions of the mask plates 14 and 15 are bent and overlapped with the center plate 9, and the overlapped portion is fixed and sealed, and the cathode side is passed through the manifold 6 for supplying and discharging the oxidizing gas. The oxidizing gas is supplied to the gas flow path 12, and the fuel gas is supplied to the anode side gas flow path 13 through the fuel gas supply / discharge manifold 7, and the manifolds 6 and 7 of the center plate 9 are Small protrusions 1 formed by embossing the same shape on both the front and back sides of the peripheral part provided
7 and 18 are arranged at required intervals so that the small projections 17 and 18 keep the distance between the mask plates 14 and 15 and the center plate 9 constant, and to the gas flow paths 12 and 13. The flowing gas can be dispersed. Reference numeral 11 indicates a spacer block.

【0006】[0006]

【発明が解決しようとする課題】ところが、溶融炭酸塩
型燃料電池では、カソード2側とアノード3側のガス流
量が大きく異なる(10:1〜5:1)ことから、上記
プレス型式のセパレータ5の如く、センタープレート9
のマニホールド6,7周辺部にエンボス加工により設け
た同一形状の小突起17,18ではカソード2側とアノ
ード3側での圧力損失をバランスさせることが難しく、
カソード2とアノード3の極間差圧や電池の内外差圧の
制御が困難になり、更に、アノード3側における圧力損
失が小さくなることから、流量配分性能が悪化する問題
がある。
However, in the molten carbonate fuel cell, since the gas flow rates on the cathode 2 side and the anode 3 side are largely different (10: 1 to 5: 1), the press type separator 5 described above is used. Like the center plate 9
It is difficult to balance the pressure loss on the cathode 2 side and the anode 3 side with the small protrusions 17 and 18 of the same shape provided by embossing around the manifolds 6 and 7,
It becomes difficult to control the inter-electrode differential pressure between the cathode 2 and the anode 3 and the internal and external differential pressure of the battery, and further, the pressure loss on the anode 3 side becomes small, so that there is a problem that the flow distribution performance deteriorates.

【0007】一方、エンボス状の小突起17,18に代
えて、コルゲート板の如き形状をプレス加工で形成する
型式もあるが、その場合、ガスの幅方向(ガスの流通方
向と直角な方向)への拡散が妨げられるため、やはり流
量配分性能に問題がある。
On the other hand, instead of the embossed small protrusions 17 and 18, there is also a type in which a shape such as a corrugated plate is formed by pressing, but in that case, in the gas width direction (direction perpendicular to the gas flow direction). However, there is still a problem with the flow distribution performance because the diffusion to the air flow is hindered.

【0008】そこで、本発明は、カソード側とアノード
側の圧力損失をバランスさせることができて、極間差圧
の制御と流量配分性能の向上を図ることができるような
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 provides a fuel cell separator which can balance the pressure loss on the cathode side and the anode side, and can control the differential pressure between electrodes and improve the flow distribution performance. Is what you are trying to do.

【0009】[0009]

【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、センタープレートの周辺部を除く中央部
分の表裏に、カソード側ガス流路とアノード側ガス流路
を形成し、上記センタープレートの周辺部に設けた酸化
ガス給排用のマニホールドと上記カソード側ガス流路と
を酸化ガスが流れるように連通させると共に、上記セン
タープレートの周辺部に設けた燃料ガス給排用のマニホ
ールドと上記アノード側ガス流路とを燃料ガスが流れる
ように連通させてある燃料電池用セパレータにおいて、
上記センタープレートの酸化ガス給排用のマニホールド
とカソード側ガス流路との間を連絡するガス流路面に小
さい突起を配列すると共に、上記センタープレートの燃
料ガス給排用のマニホールドとアノード側ガス流路との
間を連絡するガス流路面に、燃料ガスの流れを遮る面積
を大きくした広幅の突起を配列した構成とする。
In order to solve the above-mentioned problems, the present invention forms a cathode-side gas flow path and an anode-side gas flow path on the front and back sides of the central portion of the center plate excluding the peripheral portion, A manifold for supplying and discharging an oxidizing gas, which is provided in the peripheral portion of the center plate, is connected to the cathode-side gas passage so that the oxidizing gas flows, and a manifold for supplying and discharging a fuel gas, which is provided in the peripheral portion of the center plate. In the fuel cell separator in which the anode side gas flow path and the fuel gas are communicated so that the fuel gas flows,
Small projections are arranged on the gas flow path surface that connects between the oxidizing gas supply / exhaust manifold of the center plate and the cathode side gas flow path, and the fuel gas supply / exhaust manifold of the center plate and the anode side gas flow are arranged. A wide projection having a large area for interrupting the flow of the fuel gas is arranged on the gas flow path surface that communicates with the path.

【0010】[0010]

【作用】酸化ガス給排用のマニホールドとカソード側ガ
ス流路との間のガス流路面に設けた突起は小さいので、
カソード側ガス流路へ送給される酸化ガスの流れを遮る
面積が小さくて圧力損失は小さくなる。一方、燃料ガス
給排用のマニホールドとアノード側ガス流路との間のガ
ス流路面に設けた突起は広幅であるので、アノード側ガ
ス流路へ送給される燃料ガスの流れを遮る面積が大きく
なり、圧力損失が大きくなると共に、幅方向への燃料ガ
スの拡散が容易に行われる。これによりカソード側とア
ノード側の圧力損失がバランスされる。
[Function] Since the protrusion provided on the gas flow passage surface between the oxidizing gas supply / discharge manifold and the cathode gas flow passage is small,
The area that blocks the flow of the oxidizing gas fed to the cathode gas flow path is small, and the pressure loss is small. On the other hand, since the protrusion provided on the gas flow passage surface between the fuel gas supply / discharge manifold and the anode gas flow passage has a wide width, the area for interrupting the flow of the fuel gas fed to the anode gas flow passage is small. In addition to increasing the pressure loss, the fuel gas is easily diffused in the width direction. This balances the pressure loss between the cathode side and the anode side.

【0011】[0011]

【実施例】以下、本発明の実施例を図面を参照して説明
する。
Embodiments of the present invention will be described below with reference to the drawings.

【0012】図1及び図2の(イ)(ロ)(ハ)(ニ)
は本発明の一実施例を示すもので、図4及び図5に示し
たと同様に、センタープレート9の周辺部を除く中央部
分の表裏に、カソード側ガス流路12とアノード側ガス
流路13が形成されるようにしたガス流路形成用凹凸部
10をプレス成形により設け、且つ上記センタープレー
ト9の周辺部に設けたマニホールド6,7により、上記
カソード側ガス流路12へ酸化ガスを流すようにすると
共に上記アノード側ガス流路13へ燃料ガスを流すよう
にしてある燃料電池用セパレータ5において、上記セン
タープレート9の酸化ガス給排用のマニホールド6とカ
ソード側ガス流路12との間を連絡するガス流路面12
aに、プレス加工により形成した円形の如き小さい突起
19を所要間隔で配列すると共に、上記センタープレー
ト9の燃料ガス給排用のマニホールド7とアノード側ガ
ス流路13との間を連絡するガス流路面13aに、プレ
ス加工により形成した長円形の如き広幅の突起20を所
要間隔で配列して、マニホールド7からアノード側ガス
流路13へ送給される酸化ガスの流れを幅方向へ拡散さ
せられるようにする。
1 (a), 2 (b), (b), (c), and (d).
4 shows an embodiment of the present invention. Similar to that shown in FIGS. 4 and 5, the cathode side gas flow passage 12 and the anode side gas flow passage 13 are formed on the front and back sides of the central portion of the center plate 9 excluding the peripheral portion. The gas flow path forming concavo-convex portion 10 is formed by press molding, and the oxidizing gas is caused to flow to the cathode side gas flow path 12 by the manifolds 6 and 7 provided in the peripheral portion of the center plate 9. In the fuel cell separator 5 in which the fuel gas is made to flow to the anode side gas flow path 13, between the manifold 6 for supplying and discharging the oxidizing gas of the center plate 9 and the cathode side gas flow path 12. Gas flow path surface 12 for communicating with
Small protrusions 19 such as circles formed by press working are arranged at a predetermined distance on a, and a gas flow for connecting between the manifold 7 for fuel gas supply / discharge of the center plate 9 and the anode side gas passage 13 is provided. Wide projections 20 such as ellipses formed by press working are arranged on the road surface 13a at required intervals to diffuse the flow of the oxidizing gas fed from the manifold 7 to the anode side gas passage 13 in the width direction. To do so.

【0013】上記構成としたセパレータ5を、図3に示
す如き燃料電池のセル4の間に介在させて用いた場合、
センタープレート9の周辺部のガス流路面12a(図2
の(ロ)(ハ)(ニ)において中立線Lよりも上側部
分)には、円形の小さい突起19が配列されているた
め、マニホールド6から送給されてカソード側ガス流路
12へ向かう酸化ガスの流れがほとんど規制されること
はなく、圧力損失を低く抑えることができる。すなわ
ち、カソード側ガス流路12と連絡するガス流路面12
aの突起19は小さいので、酸化ガスの流れを遮る面積
が小さく、圧力損失が小さい。
When the separator 5 having the above structure is used between the cells 4 of the fuel cell as shown in FIG.
The gas flow path surface 12a in the peripheral portion of the center plate 9 (see FIG.
In (b), (c), and (d), since the small circular protrusions 19 are arranged on the upper side of the neutral line L, the oxidation that is fed from the manifold 6 toward the cathode-side gas flow channel 12 is performed. The gas flow is hardly regulated, and the pressure loss can be kept low. That is, the gas flow path surface 12 communicating with the cathode side gas flow path 12
Since the protrusion 19 of a is small, the area that blocks the flow of the oxidizing gas is small and the pressure loss is small.

【0014】一方、センタープレート9の周辺部のガス
流路面13a(図2の(ロ)(ハ)(ニ)において中立
線Lよりも下側部分)には、アノード側ガス流路13に
対し直角方向に延びる長円形の広幅の突起20が配列さ
れているので、マニホールド7から送給されてアノード
側ガス流路13へ向かう燃料ガスの流れが突起20に規
制されて幅方向に分配されることになり、このため、圧
力損失を確保しつつ流量配分性能を向上させることがで
きる。すなわち、アノード側ガス流路13と連絡するガ
ス流路面13aの突起20は広幅であるから、燃料ガス
の流れを遮る面積(投影面積)が大きく(圧力損失が大
きく)、且つ幅方向へのガス拡散が容易である。
On the other hand, in the gas passage surface 13a in the peripheral portion of the center plate 9 (the portion below the neutral line L in (b), (c) and (d) of FIG. 2) with respect to the anode side gas passage 13. Since the oblong wide projections 20 extending in the right angle direction are arranged, the flow of the fuel gas fed from the manifold 7 toward the anode gas flow path 13 is restricted by the projections 20 and distributed in the width direction. Therefore, the flow rate distribution performance can be improved while securing the pressure loss. That is, since the projection 20 on the gas flow path surface 13a that communicates with the anode-side gas flow path 13 is wide, the area (projected area) that blocks the flow of the fuel gas is large (pressure loss is large) and the gas in the width direction is wide. Easy to spread.

【0015】したがって、カソード2側とアノード3側
での圧力損失をバランスさせることができ、極間差圧の
制御と流量配分性能の向上を同時に図ることができる。
Therefore, the pressure loss on the cathode 2 side and the anode 3 side can be balanced, and the control of the inter-electrode differential pressure and the improvement of the flow rate distribution performance can be achieved at the same time.

【0016】なお、上記実施例ではセンタープレート9
の周辺部に設けた小さい突起19の形状を円形とした場
合を示したが、正方形等であってもよいこと、又、広幅
の突起20の形状を長円形とした場合を示したが、楕円
形や長方形等であってもよいこと、更に、実施例では、
センタープレート9自体を凹凸加工してガス流路形成用
凹凸部とした場合を示したが、センタープレート9の表
裏にガス流路形成用凹凸部としてコルゲート板を配置す
るようにしたセパレータについても同様に採用できるこ
と、その他本発明の要旨を逸脱しない範囲内において種
々変更を加え得ることは勿論である。
In the above embodiment, the center plate 9
Although the shape of the small protrusion 19 provided in the peripheral portion of the is shown as a circle, it may be a square or the like, and the shape of the wide protrusion 20 is shown as an ellipse. It may be a shape, a rectangle, or the like, and further, in the embodiment,
The case where the center plate 9 itself is processed to be uneven to form the gas flow path forming uneven portions is shown, but the same applies to a separator in which corrugated plates are arranged as the gas flow path forming uneven portions on the front and back of the center plate 9. It goes without saying that various modifications can be made without departing from the scope of the present invention.

【0017】[0017]

【発明の効果】以上述べた如く、本発明の燃料電池用セ
パレータによれば、センタープレート周辺部のカソード
側ガス流路と連絡するガス流路面に、小さい突起を、
又、アノード側ガス流路と連絡するガス流路面に広幅の
突起をそれぞれ配列して設けたので、カソード側では圧
力損失を低く抑えることができると共に、アノード側で
は圧力損失を確保しつつ流量配分性能を向上させること
ができ、これにより、部品点数を増やすことなく、プレ
ス加工によって極間差圧の制御と流量配分性能の向上を
図ることができ、比較的低コストで電池の性能向上及び
健全性向上を図ることができる、等の優れた効果を発揮
する。
As described above, according to the fuel cell separator of the present invention, a small protrusion is formed on the gas flow passage surface communicating with the cathode side gas flow passage in the peripheral portion of the center plate.
In addition, since wide projections are arranged on the gas flow path surface that communicates with the anode gas flow path, pressure loss can be kept low on the cathode side and flow rate can be distributed while ensuring pressure loss on the anode side. It is possible to improve the performance, and by doing this, it is possible to control the differential pressure between electrodes and improve the flow distribution performance by press working without increasing the number of parts, and to improve the battery performance and soundness at a relatively low cost. It exhibits excellent effects such as improving the properties.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の燃料電池用セパレータの一実施例を示
す一部切断平面図である。
FIG. 1 is a partially cutaway plan view showing an embodiment of a fuel cell separator of the present invention.

【図2】図1のA部を拡大して示すもので、(イ)はセ
ンタープレートの平面図、(ロ)は(イ)のB−B矢視
図、(ハ)は(イ)のC−C矢視図、(ニ)は(イ)の
D−D矢視図である。
FIG. 2 is an enlarged view of a portion A of FIG. 1, in which (a) is a plan view of the center plate, (b) is a view taken along the line BB of (a), and (c) is (a). C-C arrow view, (d) is a DD arrow view of (a).

【図3】溶融炭酸塩型燃料電池の一例を示す概略図であ
る。
FIG. 3 is a schematic view showing an example of a molten carbonate fuel cell.

【図4】プレス型式のセパレータの一例を示す一部切断
平面図である。
FIG. 4 is a partially cut plan view showing an example of a press type separator.

【図5】図4のE方向拡大矢視図である。5 is an enlarged arrow view in the E direction of FIG.

【符号の説明】[Explanation of symbols]

2 カソード 3 アノード 5 セパレータ 6 酸化ガス給排用のマニホールド 7 燃料ガス給排用のマニホールド 9 センタープレート 12 カソード側ガス流路 12a ガス流路面 13 アノード側ガス流路 13a ガス流路面 19 突起 20 突起 2 cathode 3 anode 5 separator 6 manifold for supplying / discharging oxidizing gas 7 manifold for supplying / discharging fuel gas 9 center plate 12 cathode gas flow path 12a gas flow surface 13 anode gas flow path 13a gas flow surface 19 projection 20 projection

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 センタープレートの周辺部を除く中央部
分の表裏に、カソード側ガス流路とアノード側ガス流路
を形成し、上記センタープレートの周辺部に設けた酸化
ガス給排用のマニホールドと上記カソード側ガス流路と
を酸化ガスが流れるように連通させると共に、上記セン
タープレートの周辺部に設けた燃料ガス給排用のマニホ
ールドと上記アノード側ガス流路とを燃料ガスが流れる
ように連通させてある燃料電池用セパレータにおいて、
上記センタープレートの酸化ガス給排用のマニホールド
とカソード側ガス流路との間を連絡するガス流路面に小
さい突起を配列すると共に、上記センタープレートの燃
料ガス給排用のマニホールドとアノード側ガス流路との
間を連絡するガス流路面に、燃料ガスの流れを遮る面積
を大きくした広幅の突起を配列したことを特徴とする燃
料電池用セパレータ。
1. A manifold for supplying and discharging an oxidizing gas, wherein a cathode side gas flow path and an anode side gas flow path are formed on the front and back of a central portion excluding the peripheral portion of the center plate, and which is provided in the peripheral portion of the center plate. The cathode-side gas flow channel is connected so that the oxidizing gas flows, and the manifold for fuel gas supply and discharge provided in the peripheral portion of the center plate and the anode-side gas flow channel are connected so that the fuel gas flows. In the fuel cell separator that has been made,
Small projections are arranged on the gas flow path surface that connects between the oxidizing gas supply / exhaust manifold of the center plate and the cathode side gas flow path, and the fuel gas supply / exhaust manifold of the center plate and the anode side gas flow are arranged. A fuel cell separator, characterized in that wide projections having a large area for interrupting the flow of fuel gas are arranged on a gas flow path surface that communicates with a passage.
JP33986393A 1993-12-07 1993-12-07 Fuel cell separator Expired - Fee Related JP3265782B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33986393A JP3265782B2 (en) 1993-12-07 1993-12-07 Fuel cell separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33986393A JP3265782B2 (en) 1993-12-07 1993-12-07 Fuel cell separator

Publications (2)

Publication Number Publication Date
JPH07161366A true JPH07161366A (en) 1995-06-23
JP3265782B2 JP3265782B2 (en) 2002-03-18

Family

ID=18331544

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33986393A Expired - Fee Related JP3265782B2 (en) 1993-12-07 1993-12-07 Fuel cell separator

Country Status (1)

Country Link
JP (1) JP3265782B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001013441A3 (en) * 1999-08-16 2001-06-07 Allied Signal Inc Fuel cell having improved condensation and reaction product management capabilities
JP2003077497A (en) * 2001-09-06 2003-03-14 Nippon Soken Inc Fuel cell separator
WO2003071625A3 (en) * 2002-02-25 2003-12-04 Ballard Power Systems Method of fabricating fluid flow field plates

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001013441A3 (en) * 1999-08-16 2001-06-07 Allied Signal Inc Fuel cell having improved condensation and reaction product management capabilities
US6635378B1 (en) 1999-08-16 2003-10-21 Hybrid Power Generation System, Llc Fuel cell having improved condensation and reaction product management capabilities
KR100697480B1 (en) * 1999-08-16 2007-03-20 얼라이드시그날 인코퍼레이티드 Fuel cell having improved condensation and reaction product management capabilities
JP2003077497A (en) * 2001-09-06 2003-03-14 Nippon Soken Inc Fuel cell separator
WO2003071625A3 (en) * 2002-02-25 2003-12-04 Ballard Power Systems Method of fabricating fluid flow field plates
US6818165B2 (en) 2002-02-25 2004-11-16 Ballard Power Systems Inc. Method of fabricating fluid flow field plates

Also Published As

Publication number Publication date
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