JPS63226885A - Fuel cell - Google Patents

Fuel cell

Info

Publication number
JPS63226885A
JPS63226885A JP62060677A JP6067787A JPS63226885A JP S63226885 A JPS63226885 A JP S63226885A JP 62060677 A JP62060677 A JP 62060677A JP 6067787 A JP6067787 A JP 6067787A JP S63226885 A JPS63226885 A JP S63226885A
Authority
JP
Japan
Prior art keywords
separator
gas
electrolyte
electrolyte plate
passage holes
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
Application number
JP62060677A
Other languages
Japanese (ja)
Inventor
Toshiya Matsuyama
松山 俊哉
Minoru Hosaka
保坂 実
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 JP62060677A priority Critical patent/JPS63226885A/en
Publication of JPS63226885A publication Critical patent/JPS63226885A/en
Pending 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
    • 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 prevent a local cell from being formed and reduce the loss of an electrolyte and local corrosion by providing electrolyte plates for wet sealing and electrolyte plates for each electrode section face to face for individual gas passage holes at the periphery of a separator. CONSTITUTION:Wet sealing electrolyte plates 1b of passage holes 5, 7 feeding the oxidation gas and wet sealing electrolyte plates 1b of passage holes 6, 8 feeding the fuel gas are independently provided separately from each other at the periphery of each cell, and the wet sealing electrolyte plates lb of the passage holes are independent from electrolyte plates 1a for electrode sections. Thereby, even if the wet sealing electrolyte plates 1b of the passage holes 5, 7 of the oxidation gas and the wet sealing electrolyte plates 1b of the passage holes 6, 8 of the fuel gas are brought into contact with a separator 4 and the carbonate in the electrolyte plates 1b reaches the separator 4, no positive electrode section and negative electrode section are generated on the surface of the separator 4 to cause a short circuit. Accordingly, a local cell is prevented from being formed on the surface of the separator 4.

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に関
するもので、特に、溶融炭酸塩型の燃料電池に関するも
のである。
Detailed Description of the Invention [Field of Industrial Application] The present invention relates to a fuel cell used in the energy sector that directly converts the chemical energy of fuel into electrical energy, and in particular relates to a molten carbonate type fuel cell. It is something.

[従来の技術] 現在までに提案されている溶融炭酸塩型燃料電池として
は、第3図に示す如きものがある。
[Prior Art] Among the molten carbonate fuel cells that have been proposed to date, there is one as shown in FIG.

すなわち、溶融炭酸塩を多孔質物質に浸み込ませてなる
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で両面から挾み、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■とし、各セルエをセパレータ4を介して多層に
積層した後、所定の締付力で締め付けてスタックとする
ようにしたものがある。
That is, an electrolyte plate (tile) 1 made of porous material impregnated with molten carbonate is sandwiched between a cathode (oxygen electrode) 2 and an anode (fuel electrode) 3 from both sides, and an oxidizing gas OG is placed on the cathode 2 side. At the same time, fuel gas FG is supplied to the anode 3 side.
One cell (■) is one in which electricity is generated by the potential difference generated between the cathode 2 and anode 3 by supplying There is one that can be tightened with force to form a stack.

上記の如き構成を有する燃料電池で、図示の如き内部マ
ニホールド型の場合には、電解質板1やセパレータ4の
周辺部には酸化ガスOG及び燃料ガス「Gの供給側流路
孔5及び6と、排出側流路孔7及び8が複数個設けてあ
り、電解質板1を挾んで酸化ガスOGと燃料ガスFGが
流れるようにしてあり、上記各ガスの流路孔5,6,7
.8周辺のウェットシール部ではガス洩れがないように
しておる。
In a fuel cell having the above configuration, in the case of an internal manifold type as shown in the figure, there are supply side flow passage holes 5 and 6 for oxidizing gas OG and fuel gas "G" in the peripheral areas of the electrolyte plate 1 and separator 4. , a plurality of discharge side flow passage holes 7 and 8 are provided, and the electrolyte plate 1 is sandwiched between them so that the oxidizing gas OG and the fuel gas FG can flow.
.. The wet seal area around 8 is designed to prevent gas leakage.

内部マニホールド型の燃料電池における従来の電解質板
1は、通常、第4図に示す如く周辺部のウェットシール
部へに前記の如き酸化ガス及び燃料ガスの流路孔5,6
や7,8が設けてあって、電極が接触する部分である電
極部8とは一体のものとしである。
A conventional electrolyte plate 1 in an internal manifold type fuel cell usually has the above-mentioned flow passage holes 5 and 6 for oxidizing gas and fuel gas in the wet seal part at the periphery, as shown in FIG.
7 and 8 are provided, and are integral with an electrode portion 8, which is a portion in contact with the electrodes.

[発明が解決しようとする問題点] そのため、電解質板1のウェットシール部へに含浸され
ている炭酸塩が接する金属面たるセパレータ4の局部に
おいて、酸化ガスを流す流路孔5又は7と、燃料ガスを
流す流路孔6又は8と、酸化ガス及び燃料ガスが流れる
セパレータ4のガス通路との間で陽極部と陰極部が生起
して局部電池が構成され、炭酸塩が陰極側であるカソー
ドガス(酸化ガス)側へ析出される。
[Problems to be Solved by the Invention] Therefore, in a local part of the separator 4, which is a metal surface that is in contact with the carbonate impregnated into the wet seal portion of the electrolyte plate 1, the flow passage hole 5 or 7 through which the oxidizing gas flows, An anode part and a cathode part are formed between the flow passage hole 6 or 8 through which the fuel gas flows and the gas passage of the separator 4 through which the oxidizing gas and the fuel gas flow, forming a local battery, and the carbonate is on the cathode side. It is deposited on the cathode gas (oxidizing gas) side.

その結果、上記析出された炭酸塩により電解質板1に含
浸されている炭酸塩中の陽極部が引かれて流出させられ
、電解質(炭酸塩)の損失の原因となっていた。又、電
解質板1のウェットシール部Aとセパレータ4の周辺部
との接触する面積も広いことから、金属面と炭酸塩との
反応が起り易く腐食を生じ易かった。
As a result, the anode portion of the carbonate impregnated in the electrolyte plate 1 is pulled and drained by the precipitated carbonate, causing loss of electrolyte (carbonate). Furthermore, since the contact area between the wet seal portion A of the electrolyte plate 1 and the peripheral portion of the separator 4 is large, a reaction between the metal surface and the carbonate is likely to occur, and corrosion is likely to occur.

そこで、本発明は、局部電池が形成されることを防止し
て電解質の損失、局部腐食を低減させるようにしようと
するものである。
Therefore, the present invention aims to prevent the formation of local batteries and reduce electrolyte loss and local corrosion.

[問題点を解決するための手段] 本発明は、上記目的を達成するために、電解質板を電極
が接触する部分に対応する大きさとして、各ガスの流路
孔にウェットシール用の電解質板を各々設置し、電解質
板を電極部分と各流路孔のウェットシール部分とに独立
させ、且つ全体をN2雰囲気中に置いた構成とする。
[Means for Solving the Problems] In order to achieve the above object, the present invention provides an electrolyte plate having a size corresponding to the portion in contact with the electrode, and an electrolyte plate for wet sealing in each gas passage hole. are installed, the electrolyte plate is separated into the electrode portion and the wet seal portion of each channel hole, and the entire structure is placed in an N2 atmosphere.

[作  用] セパレータ周辺部の各ガスの流路孔ごとにウェットシー
ル用の電解質板が各々電極部用の電解質板とは独立させ
て設けであるため、各ガスの流路孔の電解質板は互に切
り離されている。
[Function] Since the electrolyte plate for wet sealing is provided for each gas flow hole in the periphery of the separator independently from the electrolyte plate for the electrode section, the electrolyte plate for each gas flow hole is separated from each other.

そのため、セパレータと接触する各流路孔のウェットシ
ール用電解質板の炭酸塩がセパレータに接触しても、燃
料ガス側と酸化ガス側との間で炭酸イオンの移動が抑制
され、局部電池は形成されない。又、セパレータと接触
する電解質板の面積が小さいため、腐食も少ない。
Therefore, even if the carbonate in the wet seal electrolyte plate of each channel hole that comes into contact with the separator comes into contact with the separator, the movement of carbonate ions between the fuel gas side and the oxidizing gas side is suppressed, and a local battery is formed. Not done. Furthermore, since the area of the electrolyte plate that comes into contact with the separator is small, corrosion is less likely.

[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図及び第2図は本発明の一実施例を示すもので、第
3図及び第4図の如く、周辺部の一側に酸化ガスOGの
供給流路孔5と燃料ガスFGの供給側流路孔6を交互に
複数個設けると共に、周辺部の他側に酸化ガスOGの排
出側法路孔7と燃料ガスFGの排出側流路孔8を交互に
複数個設け、各セルの電解質板1を挾んで酸化ガスOG
と燃料ガスFGが平行流となるようにした型式の内部マ
ニホールド型燃料電池に適用した場合を示している。
FIGS. 1 and 2 show an embodiment of the present invention, and as shown in FIGS. 3 and 4, an oxidizing gas OG supply passage hole 5 and a fuel gas FG supply passage hole 5 are provided on one side of the peripheral portion. A plurality of side flow passage holes 6 are provided alternately, and a plurality of discharge side flow passage holes 7 for oxidizing gas OG and discharge side flow passage holes 8 for fuel gas FG are alternately provided on the other side of the periphery. Oxidizing gas OG with electrolyte plate 1 in between
This figure shows a case where the fuel cell is applied to an internal manifold type fuel cell in which the fuel gas FG and the fuel gas FG flow in parallel.

本発明の燃料電池は、図示の如く、セパレータ4の周辺
部に設ける酸化ガス及び燃料ガスの給排側の流路孔5,
6や7,8の部分のみ、ウェブ1〜シール用の電解質板
1bを筒形に各々形成し、両面にカソード2及びアノー
ド3を接触させる電解質板1aを、該カソード2及びア
ノード3の各電極に対応した大きざとし、該電極部用の
電解質板1aと各ガスの流路孔のウェットシール用の各
電解質板1bとは互に独立したものとし、セパレータ4
の周辺部には上記各電解質板1b以外には電解質板°が
ないようにする。
As shown in the figure, the fuel cell of the present invention includes flow passage holes 5 on the supply and discharge side for oxidizing gas and fuel gas, which are provided in the periphery of the separator 4;
Only in parts 6, 7, and 8, the web 1 to the electrolyte plate 1b for sealing are formed in a cylindrical shape, and the electrolyte plate 1a, which contacts the cathode 2 and the anode 3 on both sides, is connected to each electrode of the cathode 2 and anode 3. The electrolyte plate 1a for the electrode portion and each electrolyte plate 1b for wet sealing the flow path holes of each gas are made independent from each other, and the separator 4
There should be no electrolyte plates other than the above-mentioned electrolyte plates 1b around the area.

燃料電池として組み立てるときは、電極部用の小さい電
解質板1aの両面を第3図に示す従来方式と同様にカソ
ード2とアノード3とで挾み、カソード2側に酸化ガス
を、又、アノード3側に燃料ガスをそれぞれ流すように
してなる1セルをセパレータ4を介して多層に積層させ
、且つ各ガスの流路孔5,6,7.8のウェットシール
部に、独立した筒形の電解質板1bを各々設置し、全体
をN2が満たされた容器内に収納してN、雰囲気中に置
くようにする。
When assembling a fuel cell, both sides of a small electrolyte plate 1a for electrode parts are sandwiched between a cathode 2 and an anode 3 as in the conventional method shown in FIG. One cell is stacked in multiple layers with a separator 4 in between so that fuel gas flows through each side, and an independent cylindrical electrolyte is placed in the wet seal portion of each gas passage hole 5, 6, 7.8. Each plate 1b is installed, and the whole is housed in a container filled with N2 and placed in a N2 atmosphere.

各セルの周辺部は、第1図及び第2図に示す如く、酸化
ガスを流す流路孔5又は7のウェットシール用電解質板
1bと、燃料ガスを流ず流路孔6又は8のウェットシー
ル用電解質板1bとが互に全く切り離されて独立してお
り、且つ第1図の如く、各流路孔のウェットシール用の
電解質板1bは、電極部用の電解質板1aからも独立し
ている構成としであるため、酸化ガスの流路孔5.7の
ウェットシール用電解質板1bと燃料ガスの流路孔6,
8のウェットシール用電解質板1bがセパレータ4と接
触してこれら各電解質板1b中の炭酸塩がセパレータ4
に接しても、セパレータ4の表面に陽極部と陰極部が生
じて短絡することはなく、セパレータ4の表面での局部
電池の形成は阻止される。又、仮りに局部電池が形成さ
れたとしても、周辺部の各流路孔ウェットシール用の電
解質板1bと電極部用の電解質板1aとが前記した如く
独立しているので、電極部用の電解質板1a中の電解質
が酸化ガスの流路孔に移動することによる損失はない。
As shown in FIGS. 1 and 2, the periphery of each cell consists of an electrolyte plate 1b for wet sealing in the flow passage hole 5 or 7 through which oxidizing gas flows, and a wet sealing electrolyte plate 1b in the flow passage hole 6 or 8 through which the fuel gas does not flow. The electrolyte plates 1b for sealing are completely separated and independent from each other, and as shown in FIG. Since the configuration is such that the wet sealing electrolyte plate 1b of the oxidizing gas flow path hole 5.7 and the fuel gas flow path hole 6,
The wet sealing electrolyte plates 1b of 8 come into contact with the separator 4, and the carbonate in each of these electrolyte plates 1b is released into the separator 4.
Even if the separator 4 comes into contact with the separator 4, an anode portion and a cathode portion will not be formed on the surface of the separator 4 and a short circuit will occur, and the formation of a local battery on the surface of the separator 4 is prevented. Furthermore, even if a local battery is formed, the electrolyte plate 1b for wet-sealing each channel hole in the peripheral area and the electrolyte plate 1a for the electrode part are independent as described above. There is no loss due to the electrolyte in the electrolyte plate 1a moving to the oxidizing gas flow path holes.

又、セパレータ4の周辺部には、上記各カスの流路孔ウ
ェットシール用の電解質板1bが接触しているだけでお
るため、電解質板1bと金属製のセパレータ4とが接触
する面積が小さく、それだけ腐食も低減させることがで
きる。
In addition, since the electrolyte plate 1b for wet sealing the channel holes of each of the scum is in contact with the periphery of the separator 4, the contact area between the electrolyte plate 1b and the metal separator 4 is small. , corrosion can be reduced accordingly.

なお、上記実施例では、周辺部の一側に酸化ガスと燃料
ガスの供給側流路孔5,6があり、周辺部の反対側に酸
化ガスと燃料ガスの排出側流路孔7,8があり、酸化ガ
スと燃料ガスが電解質板を挾んで平行流となる場合を示
したが、ガスの流れを、上記平行流以外に対向流、直交
流となるようにした形式のものでも同様であること、各
ガスの流路孔の形状は図示以外のものでもよいこと、そ
の他本発明の要旨を逸脱しない範囲内で種々の変更を加
え得ることは勿論である。
In the above embodiment, the oxidizing gas and fuel gas supply side passage holes 5 and 6 are provided on one side of the peripheral portion, and the oxidizing gas and fuel gas discharge side passage holes 7 and 8 are provided on the opposite side of the peripheral portion. Although we have shown the case where the oxidizing gas and the fuel gas sandwich the electrolyte plate and flow in parallel, the same can be said of the case where the gas flows are counter-flow or cross-flow in addition to the above-mentioned parallel flow. It goes without saying that the shapes of the flow passage holes for each gas may be other than those shown in the drawings, and that various other changes may be made without departing from the gist of the present invention.

[発明の効果] 以上述べた如く、本発明の燃料電池によれば、内部マニ
ホールド形の燃料電池において、周辺部に設けられる酸
化ガスの流路孔ウェットシール用の電解質板と燃料ガス
の流路孔ウェットシール用の電解質板とを互に全く切り
離して独立させると共に、これら各電解質板を電極部用
の電解質板からも独立させた構成とし、全体をN2雰囲
気中に置いた構成としであるので、酸化ガスの流路孔と
燃料ガスの流路孔を完全に切り離すことができて、酸化
ガス流路孔、燃料ガス流路孔、金属製セパレータ内流路
間で局部電池が形成されることがなく、電解質損失を低
減することができると共に、酸化ガスの流路孔ウェット
シール用の電解質板と燃料ガスの流路孔ウェットシール
用の電解質板とが完全に切り離されていることから、こ
れらが金属製セパレータに接触する面積を減少させるこ
とができて腐食の低減も図れ、又、シールのセパレータ
表面の平滑性に対する依存度を減らしシール効率の上昇
も期待できる、という優れた効果を奏し得る。
[Effects of the Invention] As described above, according to the fuel cell of the present invention, in an internal manifold type fuel cell, the electrolyte plate for wet-sealing the oxidizing gas passage hole provided in the peripheral portion and the fuel gas passage The electrolyte plates for hole wet sealing are completely separated from each other and made independent, and each of these electrolyte plates is also made independent from the electrolyte plate for the electrode section, and the entire structure is placed in an N2 atmosphere. , the oxidizing gas flow path hole and the fuel gas flow path hole can be completely separated, and a local battery is formed between the oxidation gas flow path hole, the fuel gas flow path hole, and the flow path in the metal separator. In addition to reducing electrolyte loss, the electrolyte plate for wet sealing the oxidizing gas flow path hole and the electrolyte plate for wet sealing the fuel gas flow path hole are completely separated. The area in contact with the metal separator can be reduced, reducing corrosion. Furthermore, the dependence of the seal on the smoothness of the separator surface can be reduced, and an increase in sealing efficiency can be expected. .

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の燃料電池における電解質板とセパレー
タとの関係を示す一例図、第2図は第1図の■−■拡大
断面図、第3図は従来の内部マニホールド型の溶融炭酸
塩型燃料電池の一例を示す切断側面図、第4図は従来の
燃料電池における電解質板の平面図でおる。 1、la、lb・・・電解質板、2・・・カソード、3
・・・アノード、4・・・セパレータ。
Fig. 1 is an example diagram showing the relationship between the electrolyte plate and the separator in the fuel cell of the present invention, Fig. 2 is an enlarged sectional view taken along ■-■ of Fig. 1, and Fig. 3 is a conventional internal manifold type molten carbonate salt. FIG. 4 is a cutaway side view showing an example of a type fuel cell, and FIG. 4 is a plan view of an electrolyte plate in a conventional fuel cell. 1, la, lb... electrolyte plate, 2... cathode, 3
...Anode, 4...Separator.

Claims (1)

【特許請求の範囲】[Claims] 1)電解質板及びセパレータの周辺部に酸化ガス用及び
燃料ガス用の各給排用流路孔を有し、且つ上記電解質板
の両面をカソードとアノードの各電極で挾持させ、カソ
ード側に酸化ガスを、アノード側に燃料ガスを各々流す
ようにしたものをセパレータを介して積層してなる内部
マニホールド型の燃料電池において、上記電解質板を、
電極が接触する電極部用の電解質板と、各ガスの流路孔
部分のウエットシール用の各電解質板とに切り離して互
に独立させ、且つ全体をN_2雰囲気中に置いてなるこ
とを特徴とする燃料電池。
1) The electrolyte plate and the separator have flow passage holes for supplying and discharging oxidizing gas and fuel gas in the periphery of the plate, and both sides of the electrolyte plate are held between the cathode and anode electrodes, so that the oxidation gas is formed on the cathode side. In an internal manifold type fuel cell formed by stacking gas and fuel gas to the anode side through a separator, the electrolyte plate is
It is characterized by having an electrolyte plate for the electrode part that the electrodes contact, and each electrolyte plate for wet sealing the flow path hole part of each gas separated and made independent from each other, and the whole being placed in an N_2 atmosphere. fuel cell.
JP62060677A 1987-03-16 1987-03-16 Fuel cell Pending JPS63226885A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62060677A JPS63226885A (en) 1987-03-16 1987-03-16 Fuel cell

Applications Claiming Priority (1)

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JP62060677A JPS63226885A (en) 1987-03-16 1987-03-16 Fuel cell

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JPS63226885A true JPS63226885A (en) 1988-09-21

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4942099A (en) * 1988-11-28 1990-07-17 Kabushiki Kaisha Toshiba Fuel cell
US5532073A (en) * 1993-11-29 1996-07-02 Kabushiki Kaisha Toshiba Fuel cell

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4942099A (en) * 1988-11-28 1990-07-17 Kabushiki Kaisha Toshiba Fuel cell
US5532073A (en) * 1993-11-29 1996-07-02 Kabushiki Kaisha Toshiba Fuel cell

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