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JP2001068132A - Current collector plate and solid electrolyte fuel cell using the same - Google Patents

Current collector plate and solid electrolyte fuel cell using the same

Info

Publication number
JP2001068132A
JP2001068132A JP23828799A JP23828799A JP2001068132A JP 2001068132 A JP2001068132 A JP 2001068132A JP 23828799 A JP23828799 A JP 23828799A JP 23828799 A JP23828799 A JP 23828799A JP 2001068132 A JP2001068132 A JP 2001068132A
Authority
JP
Japan
Prior art keywords
flat
plate
cell
metal
solid electrolyte
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.)
Withdrawn
Application number
JP23828799A
Other languages
Japanese (ja)
Inventor
Yuichi Hishinuma
祐一 菱沼
Yoshio Matsuzaki
良雄 松崎
Hisataka Yakabe
久孝 矢加部
Takashi Ogiwara
崇 荻原
Kentaro Ito
健太郎 伊東
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.)
Tokyo Gas Co Ltd
Original Assignee
Tokyo Gas Co Ltd
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 Tokyo Gas Co Ltd filed Critical Tokyo Gas Co Ltd
Priority to JP23828799A priority Critical patent/JP2001068132A/en
Publication of JP2001068132A publication Critical patent/JP2001068132A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • 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

  • Fuel Cell (AREA)

Abstract

PROBLEM TO BE SOLVED: To secure electric conduction between flat unit cells and provide a fuel cell in which no excessive load can be exerted on the flat unit cell due to a thermal stress or the like. SOLUTION: A solid electrolyte fuel cell 4 comprises a flat unit cell 6, a first spacer 8, a second spacer 10 and metal thin plates 11, 12 forming current collecting plates. The metal thin plate 11 is provided with projections projecting at the obverse and reverse by pressing, and the metal thin plate 12 is provided with projections projecting at the obverse and reverse. The projection is formed in such a height as to be brought into contact with the surface of a fuel or air electrode when the solid electrolyte fuel cell 4 is laminated. Consequently, the metal thin plate 12 defines a fuel gas passing portion and an oxidant gas passing portion. The projections of the metal thin plate 11 is brought into elastic contact with the fuel electrode of the solid electrolyte fuel cell 4 and the air electrode of the other solid electrolyte fuel cell 4, thereby achieving the electric conduction between the electrodes.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、平板型単電池とセ
パレータとを積層した固体電解質燃料電池に関し、特に
平板型単電池間相互の通電、各ガスの通路の分離を確実
にし、かつ温度変化等に起因する熱応力による破損を防
止した固体電解質燃料電池に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a solid electrolyte fuel cell in which a flat plate cell and a separator are stacked, and more particularly, to ensuring mutual energization between the flat plate cells, separation of gas passages, and temperature change. The present invention relates to a solid electrolyte fuel cell that is prevented from being damaged by thermal stress caused by the above.

【0002】[0002]

【従来の技術】最近、例えば空気と水素をそれぞれ、酸
化剤ガスおよび燃料ガスとして、燃料が本来持っている
化学エネルギーを直接電気エネルギーに変換する燃料電
池が、省資源、環境保護の観点から注目されており、特
に固体電解質燃料電池は発電効率が高く、廃熱を有効に
利用できるなど多くの利点を有するため研究、開発が進
んでいる。
2. Description of the Related Art Recently, fuel cells which directly convert chemical energy inherent in fuel into electric energy by using, for example, air and hydrogen as oxidizing gas and fuel gas, respectively, have attracted attention from the viewpoint of resource saving and environmental protection. Research and development are progressing because solid electrolyte fuel cells have many advantages such as high power generation efficiency and effective use of waste heat.

【0003】図13に、従来の内部マニホールド方式の
平板型固体電解質燃料電池100を示す。
FIG. 13 shows a conventional plate type solid electrolyte fuel cell 100 of an internal manifold system.

【0004】固体電解質燃料電池に燃料ガスと酸化剤ガ
スとを供給するため、固体電解質燃料電池のセパレータ
等にそれぞれのガスの給排気孔を設け、これらの孔から
各平板型単電池の各電極面に各ガスを給排気するように
したものを内部マニホールド形式と称している。
In order to supply the fuel gas and the oxidizing gas to the solid electrolyte fuel cell, gas supply / exhaust holes for each gas are provided in a separator or the like of the solid electrolyte fuel cell. The one that supplies and exhausts each gas to and from the surface is called an internal manifold type.

【0005】図13に示すように平板型固体電解質燃料
電池100は、イットリアなどをドープしたジルコニア
焼結体(YSZ)からなる平板型固体電解質層102の
両面に、それぞれ(La、Sr)MnO3 の空気極1
04と、Ni/YSZサーメットの燃料極106とを配
置してなる平板型単電池108と、隣接する平板型単電
池108同士を電気的に直列に接続し、かつ平板型単電
池108に燃料ガスと酸化剤ガスとを分配するセパレー
タ110からなり、メッシュ状の金属115をセパレー
タ110と燃料極106との間に配置し、又、セパレー
タ110と空気極104との間に接続層117を配置
し、セパレータ110と燃料極106、および空気極1
04とを導通させ、また、側面にシール材119を設け
閉鎖させている。
As shown in FIG. 13, a flat solid electrolyte fuel cell 100 has a flat solid electrolyte layer 102 made of a zirconia sintered body (YSZ) doped with yttria or the like. Air electrode 1
04 and the Ni / YSZ cermet fuel electrode 106 are arranged, and the flat plate cells 108 adjacent to each other are electrically connected in series. A mesh metal 115 is disposed between the separator 110 and the fuel electrode 106, and a connection layer 117 is disposed between the separator 110 and the air electrode 104. , Separator 110, fuel electrode 106, and air electrode 1
04, and a seal member 119 is provided on the side surface to close the cover.

【0006】そして、平板型固体電解質燃料電池100
を交互に積層し、通路114からそれぞれ酸化剤ガスと
燃料ガスを導入し、各平板型単電池108の空気極10
4、および燃料極106の面にこれら酸化剤ガスと燃料
ガスを接触させることにより起電力を発生させ、直列に
積層した固体電解質燃料電池100から出力するように
している。
[0006] The flat solid electrolyte fuel cell 100
Are alternately stacked, and an oxidizing gas and a fuel gas are introduced from the passages 114, respectively.
4, and by bringing the oxidant gas and the fuel gas into contact with the surface of the fuel electrode 106, an electromotive force is generated, and output from the solid electrolyte fuel cells 100 stacked in series.

【0007】[0007]

【発明が解決しようとする課題】従来セパレータ110
の集電面は、機械加工等により平面に形成しているが、
平板型単電池108は、製作時に生じた反りや歪みを有
し、その歪みは平板型単電池108の材質等の関係から
機械的な加工を行なって完全な平面に修正することが困
難である。そのため、セパレータ110を平板型単電池
108に取り付けた場合、平板型単電池108がセパレ
ータ110の集電面と面全体で接触するのではなく、多
くとも3点の点接触となって良好な電気的な接続状態が
得られないことがある。そこで、平板型単電池108を
変形させるか、あるいはセパレータ110の集電面と平
板型単電池108の間に導電性の接着剤等を用いて互い
に面の接触を行なうようにする方法が考えられるが、導
電性の接着剤を用いて接合させると、それぞれの部材の
熱膨張特性が異なるため、運転時、停止時の温度変化に
よる熱変形が生じ、特にセパレータ110の剛性が高い
ため発生した応力が平板型単電池108に大きくかか
り、平板型単電池108が破損することがある。更にこ
の場合、加工費が高く、しかも重量が重くなるという問
題がある。
SUMMARY OF THE INVENTION Conventional separator 110
The current collecting surface is formed flat by machining or the like,
The flat plate cell 108 has a warp or distortion generated at the time of manufacturing, and it is difficult to correct the distortion to a perfect plane by performing mechanical processing due to the material of the flat plate cell 108 or the like. . Therefore, when the separator 110 is attached to the flat cell 108, the flat cell 108 does not come into contact with the current collecting surface of the separator 110 on the entire surface, but has at most three points of contact, thereby providing good electric power. Connection state may not be obtained. Therefore, a method is considered in which the flat cell 108 is deformed, or the surfaces of the current collecting surface of the separator 110 and the flat cell 108 are brought into contact with each other using a conductive adhesive or the like. However, when joined by using a conductive adhesive, the thermal expansion characteristics of the respective members are different, so that during operation, thermal deformation due to a temperature change at the time of stop occurs, and particularly, the stress generated due to high rigidity of the separator 110 is generated. Is greatly applied to the flat cell 108, and the flat cell 108 may be damaged. Further, in this case, there is a problem that the processing cost is high and the weight is heavy.

【0008】また、平板型単電池108を複数積層した
際、締め付けの荷重がセラミック製のセパレータ110
を介して平板型単電池108にかかる構造であり、温度
変動により締め付け力が変化し荷重が過大になったとき
セパレータ110や平板型単電池108が破壊してしま
うことがある。更に、変形に対処するため平板型単電池
108を電気的に接続させる導通用の金属115を強固
にしなければならず、これによっても平板型単電池10
8に荷重がかかってしまい、熱応力等により平板型単電
池108の破損等を引き起こすことが考えられる。
When a plurality of flat plate cells 108 are stacked, the tightening load is increased by a ceramic separator 110.
The separator 110 and the flat cell 108 may be broken when the tightening force changes due to temperature fluctuation and the load becomes excessive when the load is excessive. Further, in order to cope with the deformation, the conducting metal 115 for electrically connecting the flat cell 108 must be strengthened.
It is conceivable that a load is applied to the plate 8 and the flat cell 108 is damaged by thermal stress or the like.

【0009】[0009]

【課題を解決するための手段】本発明では、上記課題を
解決するため次のように燃料電池を構成した。
According to the present invention, a fuel cell is constructed as follows in order to solve the above-mentioned problems.

【0010】すなわち、金属平板と金属薄板とにより集
電板を形成し、積層した各平板型単電池間に金属平板を
設けて平板型単電池の燃料通路と空気通路を分離し、か
つ前記金属平板に、表面に凹凸を備えた金属薄板を取り
付け、金属薄板に対向する平板型単電池の空気極あるい
は燃料極とに弾性をもって電気的に接続させることとし
た。
That is, a current collector plate is formed by a metal flat plate and a thin metal plate, and a metal flat plate is provided between the stacked flat cell units to separate a fuel passage and an air passage of the flat unit cell. A thin metal plate having irregularities on its surface is attached to the flat plate, and is electrically connected to the air electrode or the fuel electrode of the flat plate cell facing the thin metal plate with elasticity.

【0011】このように金属平板と金属薄板とにより集
電板を形成し、積層した各平板型単電池間に集電板を設
けたことにより、金属平板の両側に設けられた金属薄板
により空気極と燃料極が良好な接触状態で確実に電気的
に接続され、また、金属薄板が弾性をもって平板型単電
池に接することから平板型単電池にかかる荷重を緩和で
き、温度変動等による応力を原因とした平板型単電池の
破損を防止できる。
As described above, the current collecting plate is formed by the metal flat plate and the metal thin plate, and the current collecting plate is provided between the stacked flat unit cells, so that the air is formed by the metal thin plates provided on both sides of the metal flat plate. The electrode and fuel electrode are reliably electrically connected in a good contact state, and since the thin metal plate is elastically in contact with the flat cell, the load on the flat cell can be reduced, and stress due to temperature fluctuations etc. can be reduced. It is possible to prevent the damage of the flat plate type cell which is the cause.

【0012】更に、各平板型単電池が金属平板を介して
積層されることから、燃料通路と空気通路を完全に分離
でき、かつスタック全体の歪みや単電池の反りなどに起
因する局所的な応力集中を防止できる。
Further, since the flat plate cells are stacked via a metal plate, the fuel passage and the air passage can be completely separated from each other, and local distortion caused by distortion of the entire stack, warpage of the unit cell, and the like can be achieved. Stress concentration can be prevented.

【0013】[0013]

【発明の実施の形態】本発明にかかる燃料電池の通電方
法とその燃料電池の一実施形態について説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A method for energizing a fuel cell according to the present invention and an embodiment of the fuel cell will be described.

【0014】図1に、内部マニホールド方式の燃料電池
2の断面図を示す。図1は、図3における燃料電池2の
A矢視の断面図である。図1に示すように燃料電池2
は、複数の固体電解質燃料電池4を所定数積層して構成
されており、また固体電解質燃料電池4は、平板型単電
池6と、第1スペーサ8と、第2スペーサ10と、集電
板3を形成する金属薄板11及び金属平板12等から構
成されている。
FIG. 1 is a sectional view of a fuel cell 2 of an internal manifold system. FIG. 1 is a sectional view of the fuel cell 2 in FIG. As shown in FIG.
Is formed by laminating a plurality of solid electrolyte fuel cells 4 in a predetermined number, and the solid electrolyte fuel cell 4 includes a flat cell 6, a first spacer 8, a second spacer 10, 3 are formed of a metal thin plate 11 and a metal flat plate 12.

【0015】第1スペーサ8と第2スペーサ10は、図
3に示すようにほぼ正方形で、耐熱性金属で形成されて
いる。第1スペーサ8の中央には、平板型単電池6を収
容する収容部14が形成してあり、収容部14の周囲に
燃料ガス用供給通路22と、燃料ガス用排気通路24
と、酸化剤ガス用供給通路26と、酸化剤ガス用排気通
路28が形成されている。収容部14は、平板型単電池
6にほぼ等しい正方形状で、表裏貫通して形成してあ
る。燃料ガス用供給通路22と燃料ガス用排気通路2
4、及び酸化剤ガス用供給通路26と酸化剤ガス用排気
通路28は、収容部14を挟んで斜め方向に対向して形
成してあり、かつ燃料ガス用供給通路22と燃料ガス用
排気通路24は収容部14に開口している。
The first spacer 8 and the second spacer 10 are substantially square as shown in FIG. 3, and are formed of a heat-resistant metal. An accommodation portion 14 for accommodating the flat cell 6 is formed at the center of the first spacer 8, and a fuel gas supply passage 22 and a fuel gas exhaust passage 24 are provided around the accommodation portion 14.
In addition, an oxidizing gas supply passage 26 and an oxidizing gas exhaust passage 28 are formed. The accommodating portion 14 has a square shape substantially equal to that of the flat cell 6 and is formed to penetrate the front and back. Fuel gas supply passage 22 and fuel gas exhaust passage 2
The oxidizing gas supply passage 26 and the oxidizing gas exhaust passage 28 are formed diagonally opposite to each other with the housing portion 14 interposed therebetween, and the fuel gas supply passage 22 and the fuel gas exhaust passage Reference numeral 24 is open to the accommodating portion 14.

【0016】第2スペーサ10は、第1スペーサ8とほ
ぼ同形で、中央には切り欠き20が形成してあり、周囲
には燃料ガス用供給通路22と、燃料ガス用排気通路2
4と、酸化剤ガス用供給通路26と、酸化剤ガス用排気
通路28が第1スペーサ8と同様に形成されている。切
り欠き20は、平板型単電池6の空気極面より若干大き
く形成してあり、表裏貫通して形成してある。燃料ガス
用供給通路22と燃料ガス用排気通路24、及び酸化剤
ガス用供給通路26と酸化剤ガス用排気通路28は、切
り欠き20を挟んで対向して形成してあり、かつ酸化剤
ガス用供給通路26と酸化剤ガス用排気通路28が切り
欠き20に開口している。
The second spacer 10 has substantially the same shape as the first spacer 8 and has a cutout 20 formed in the center, and a fuel gas supply passage 22 and a fuel gas exhaust passage 2 around the periphery.
4, an oxidizing gas supply passage 26, and an oxidizing gas exhaust passage 28 are formed similarly to the first spacer 8. The notch 20 is formed slightly larger than the air electrode surface of the flat plate type cell 6 and penetrates the front and back. The fuel gas supply passage 22 and the fuel gas exhaust passage 24, and the oxidizing gas supply passage 26 and the oxidizing gas exhaust passage 28 are formed to face each other with the notch 20 interposed therebetween. A supply passage 26 and an oxidant gas exhaust passage 28 are open in the notch 20.

【0017】平板型単電池6は、ほぼ正方形で、YSZ
からなる平板型固体電解質層の両面にそれぞれ(La、
Sr)MnO の空気極とNi/YSZサーメットの
燃料極(いずれも図示せず)とを配置して形成してあ
る。更に平板型単電池6の表面外周部には保持薄板枠1
6が接合材17により接合してある。保持薄板枠16に
は、燃料ガス用供給通路22と、燃料ガス用排気通路2
4と、酸化剤ガス用供給通路26と、酸化剤ガス用排気
通路28が第1スペーサ8と同様に形成され、保持薄板
枠16を第1スペーサ8と第2スペーサ10で挟み込
み、平板型単電池6を第1スペーサ8と第2スペーサ1
0の間で支持する構造となっている。
The flat cell 6 has a substantially square shape and a YSZ
(La, on both sides of a flat solid electrolyte layer composed of
Sr) An air electrode of MnO 3 and a fuel electrode of Ni / YSZ cermet (both not shown) are arranged and formed. Further, the holding thin plate frame 1 is provided on the outer peripheral portion of the surface of the flat cell 6.
6 are joined by a joining material 17. The holding thin plate frame 16 has a fuel gas supply passage 22 and a fuel gas exhaust passage 2.
4, an oxidizing gas supply passage 26, and an oxidizing gas exhaust passage 28 are formed similarly to the first spacer 8, and the holding thin plate frame 16 is sandwiched between the first spacer 8 and the second spacer 10, and Battery 6 is divided into first spacer 8 and second spacer 1
It is structured to support between zero.

【0018】金属平板12は、インコネル600からな
る金属製の平板状部材であり、第1スペーサ8とほぼ同
一の外形をしており、更に周囲には燃料ガス用供給通路
22と、燃料ガス用排気通路24と、酸化剤ガス用供給
通路26と、酸化剤ガス用排気通路28が第1スペーサ
8と同様に形成されている。尚、金属平板12は、完全
な平板状でなくともよく、適宜湾曲等していてもよい。
また、金属薄板11を固定する金具等を有していてもよ
い。固定用の金具としては、例えば、抜き差し可能な凹
凸、金属薄板11の周囲を保持する突起、スライド状に
抜き差しする差し込み金具等がある。
The metal flat plate 12 is a metal flat plate made of Inconel 600, has substantially the same outer shape as the first spacer 8, and further has a fuel gas supply passage 22 and a fuel gas An exhaust passage 24, an oxidant gas supply passage 26, and an oxidant gas exhaust passage 28 are formed similarly to the first spacer 8. In addition, the metal flat plate 12 does not need to be a perfect flat plate shape and may be appropriately curved or the like.
Further, a metal fitting for fixing the metal sheet 11 may be provided. Examples of the fixing bracket include, for example, irregularities that can be inserted and removed, protrusions that hold the periphery of the thin metal plate 11, and insertion fittings that can be inserted and removed in a slide shape.

【0019】金属薄板11は、インコネル600からな
る金属板で、プレス加工等により図2に示すように表面
に突部18が形成してあり、金属平板12の表裏面にそ
れぞれ設けられ、金属平板12に金属薄板11を組み合
わせて集電板3を形成している。突部18は、図1に示
すように金属平板12とともに固体電解質燃料電池4を
積層した際、金属薄板11に対向する固体電解質燃料電
池4の燃料極もしくは空気極の表面に接触する高さを有
している。更にこの突部18は、適度な弾性を有してお
り、過大な荷重が加えられた場合は、接している燃料極
や空気極等に損傷を与えることなく、適宜変形して、荷
重を緩和するようになっている。また適度な変形復元性
も備えている。尚、金属薄板11と金属平板12は、共
に耐熱性合金であり、高温の酸素雰囲気下で表面に酸化
皮膜を形成しにくい材質であれば、上記インコネル60
0以外のものでもよい。
The metal thin plate 11 is a metal plate made of Inconel 600, and has protrusions 18 formed on the front surface as shown in FIG. 2 by pressing or the like. The current collector 3 is formed by combining the metal sheet 12 with the metal sheet 12. As shown in FIG. 1, when the solid electrolyte fuel cell 4 is stacked together with the metal flat plate 12 as shown in FIG. 1, the protrusion 18 has a height that contacts the surface of the fuel electrode or the air electrode of the solid electrolyte fuel cell 4 facing the thin metal plate 11. Have. Further, the projection 18 has a moderate elasticity, and when an excessive load is applied, the projection 18 is appropriately deformed without damaging the fuel electrode, the air electrode, etc. in contact with the projection 18 to reduce the load. It is supposed to. In addition, it has a moderate deformation restoring property. Note that the metal thin plate 11 and the metal flat plate 12 are both heat-resistant alloys. If the material is such that it is difficult to form an oxide film on the surface in a high-temperature oxygen atmosphere, the above-mentioned Inconel 60 is used.
Other than 0 may be used.

【0020】これにより、上記各部材と集電板3とを積
層すると第1スペーサ8と金属平板12により燃料極へ
燃料ガスが供給される通過部分が形成され、また第2ス
ペーサ10と金属平板12により空気極へ酸化剤ガスが
供給される通過部分が形成される。また金属薄板11に
は突部18が形成してあることから上記各通路を遮断す
ることはなく、一方の金属薄板11が固体電解質燃料電
池4の燃料極と接触し、他方の金属薄板11が固体電解
質燃料電池4に積層された他の固体電解質燃料電池4の
空気極に接触するので、積層した固体電解質燃料電池4
が1組の金属薄板11と金属平板12、すなわち集電板
3により電気的に導通される。
Thus, when the above members and the current collector plate 3 are laminated, a passage portion through which the fuel gas is supplied to the fuel electrode is formed by the first spacer 8 and the metal flat plate 12, and the second spacer 10 and the metal flat plate are formed. 12 forms a passage portion through which the oxidant gas is supplied to the air electrode. Further, since the metal sheet 11 is provided with the projection 18, the above-mentioned respective passages are not interrupted, and one of the metal sheets 11 comes into contact with the fuel electrode of the solid electrolyte fuel cell 4, and the other of the metal sheets 11 Since it contacts the air electrode of another solid electrolyte fuel cell 4 stacked on the solid electrolyte fuel cell 4, the stacked solid electrolyte fuel cell 4
Are electrically conducted by a set of the thin metal plate 11 and the flat metal plate 12, that is, the current collector plate 3.

【0021】次に燃料電池2の作用について説明する。Next, the operation of the fuel cell 2 will be described.

【0022】図1に示すように燃料電池2は、固体電解
質燃料電池4を順次積層し、図示しない締結手段により
上下方向に所定圧力で締結してある。固体電解質燃料電
池4を積層することにより、燃料ガス用供給通路22、
燃料ガス用排気通路24、酸化剤ガス用供給通路26及
び酸化剤ガス用排気通路28が連続し、それぞれの流通
路として形成される。
As shown in FIG. 1, in the fuel cell 2, solid electrolyte fuel cells 4 are sequentially stacked and fastened in a vertical direction at a predetermined pressure by fastening means (not shown). By stacking the solid electrolyte fuel cells 4, the fuel gas supply passage 22,
The fuel gas exhaust passage 24, the oxidizing gas supply passage 26, and the oxidizing gas exhaust passage 28 are continuous and formed as respective flow passages.

【0023】したがって、燃料ガス用供給通路22から
燃料ガスを流入させると、燃料ガスが各固体電解質燃料
電池4の燃料極に供給され、燃料ガス用排気通路24か
ら排気され、また酸化剤ガス用供給通路26から酸化剤
ガスを流入させると、酸化剤ガスが同様に各固体電解質
燃料電池4の空気極に供給され、酸化剤ガス用排気通路
28から排気される。
Therefore, when the fuel gas flows from the fuel gas supply passage 22, the fuel gas is supplied to the fuel electrode of each solid electrolyte fuel cell 4, exhausted from the fuel gas exhaust passage 24, and exhausted from the oxidant gas. When the oxidizing gas flows from the supply passage 26, the oxidizing gas is similarly supplied to the air electrode of each solid oxide fuel cell 4 and is exhausted from the oxidizing gas exhaust passage 28.

【0024】燃料電池2を所定の温度に上昇させた上
で、このように平板型単電池6の燃料極と空気極にそれ
ぞれ燃料ガスと空気とを供給すると、平板型単電池6で
起電力が発生し、発生した起電力は各平板型単電池6を
直列に接続する集電板3(金属薄板11、金属平板1
2、金属薄板11)を介して順次流れ、燃料電池2の出
力端子(図示せず)から電流として取り出すことができ
る。
After the fuel cell 2 is heated to a predetermined temperature and the fuel gas and the air are supplied to the fuel electrode and the air electrode of the flat cell 6 in this manner, the electromotive force is generated by the flat cell 6. Is generated, and the generated electromotive force is applied to the current collector plate 3 (the metal thin plate 11, the metal flat plate 1) for connecting the respective flat plate cells 6 in series.
2. It flows sequentially through the thin metal plate 11) and can be taken out as a current from an output terminal (not shown) of the fuel cell 2.

【0025】このように燃料電池2によれば、各固体電
解質燃料電池4が金属平板12により分離されて、燃料
ガスの通路と酸化剤ガスの通路が区画され、しかも金属
薄板11が良好な接触状態で燃料極と空気極にそれぞれ
接触しているため、効率よく電流を取り出すことができ
る。また、金属薄板11は、プレス加工により凹凸が形
成してあり、その突部18の先端が平板型単電池6の表
面に接触していることから、温度変化により各部が膨張
し、また収縮が生じても突部18の弾性変形により熱応
力を吸収して接触を保ち、各固体電解質燃料電池4間の
通電が遮断されることなく、しかも熱応力によって平板
型単電池6に破損を生じさせない。
As described above, according to the fuel cell 2, each solid electrolyte fuel cell 4 is separated by the metal flat plate 12 to partition the passage of the fuel gas and the passage of the oxidizing gas. Since the fuel electrode and the air electrode are in contact with each other in this state, current can be efficiently extracted. Further, the metal sheet 11 has irregularities formed by press working, and since the tip of the projection 18 is in contact with the surface of the flat cell 6, each part expands and contracts due to a temperature change. Even if it occurs, the elastic deformation of the projection 18 absorbs the thermal stress to maintain the contact, so that the energization between the solid electrolyte fuel cells 4 is not interrupted, and the thermal stress does not damage the flat cell 6. .

【0026】また、平板型単電池6に供給される燃料ガ
スと酸化剤ガスは金属平板12により確実に分離される
ため、内部で燃料ガスや酸化剤ガスが混合されることな
く燃料極や空気極の表面に効率良く流すことができる。
Further, the fuel gas and the oxidizing gas supplied to the flat cell 6 are reliably separated by the metal flat plate 12, so that the fuel gas and the oxidizing gas are not mixed inside and the fuel electrode and the air are not mixed. It can flow efficiently on the pole surface.

【0027】次に、金属薄板11の他の例を図を用いて
示す。
Next, another example of the metal sheet 11 will be described with reference to the drawings.

【0028】金属薄板11は、凹凸状でなく図4に示す
ように、矩形状であってもよい。このようにすると所定
幅の面で燃料極等と金属平板12とを接触させることが
できる。図7に金属薄板11を金属平板12に重ねた状
態を示す。金属薄板11を重ねる方向は図11に示すよ
うに、燃料ガス等が通過する方向に合わせて積層する。
The metal sheet 11 may have a rectangular shape as shown in FIG. In this way, the fuel electrode and the like and the metal flat plate 12 can be brought into contact with each other with a predetermined width. FIG. 7 shows a state where the metal thin plate 11 is overlaid on the metal flat plate 12. As shown in FIG. 11, the metal sheets 11 are stacked in a direction in which the fuel gas or the like passes.

【0029】また矩形状でなく、図5に示すように波型
でもよい。この場合も上記例と同様、燃料ガス等が通過
する方向に合わせて配置する。
Instead of a rectangular shape, a wave shape may be used as shown in FIG. Also in this case, similarly to the above example, they are arranged in accordance with the direction in which the fuel gas or the like passes.

【0030】更に、平面状の金属薄板11に複数の短冊
状の金属片19を図9、図10に示すように、プレス加
工等により突出させ、突出した金属片19の先端部分を
燃料極や空気極に接触させるようにしてもよい。このよ
うにプレス加工等により金属薄板11に表裏を貫通する
開口部を形成しても、金属薄板12により平板型単電池
6の間のガス通路が遮断されているため燃料ガスと酸化
剤ガスが混ざることがないので、金属薄板11を任意の
形状に加工することができる。尚、金属片19を溶接等
により取り付けてもよい。更に、金属平板12の表裏面
において、異なる形状の金属薄板11を用いてもよい。
Further, as shown in FIGS. 9 and 10, a plurality of strip-shaped metal pieces 19 are protruded from the flat metal sheet 11 by pressing or the like, and the tip of the protruded metal piece 19 is used as a fuel electrode or the like. You may make it contact an air electrode. In this way, even when the opening that penetrates the front and back sides is formed in the thin metal plate 11 by press working or the like, the gas passage between the flat plate cells 6 is blocked by the thin metal plate 12 so that the fuel gas and the oxidizing gas are Since they do not mix, the metal sheet 11 can be processed into any shape. The metal piece 19 may be attached by welding or the like. Further, the metal thin plates 11 having different shapes may be used on the front and back surfaces of the metal flat plate 12.

【0031】また、図6に示すように金属平板12の周
囲に絞り部13を形成し、この絞り部13をスペーサに
より挟持させるようにしてもよい。このようにすれば、
スペーサの密着度を向上させ、かつ熱応力の緩和を図る
ことができる。
Further, as shown in FIG. 6, a narrowed portion 13 may be formed around the metal flat plate 12, and the narrowed portion 13 may be sandwiched by spacers. If you do this,
The degree of adhesion of the spacer can be improved, and the thermal stress can be reduced.

【0032】また、平板型単電池は正方形に限らず、長
方形、円形、楕円形等形状は限定せず、また、複数の平
板型単電池を横方向に並列に設けてもよい。また、図1
2に示すように、燃料ガス用供給通路22と燃料ガス用
排気通路24を対向させ、かつ、それと直角方向に酸化
剤ガス用供給通路26と酸化剤ガス用排気通路28とを
対向させて配置し、それぞれの流通路から燃料ガスおよ
び酸化剤ガスとを直交させて燃料電池2に導入させるよ
うにしてもよい。
The shape of the flat cell is not limited to a square, and the shape is not limited to a rectangle, a circle, an ellipse or the like. A plurality of flat cells may be provided in parallel in the horizontal direction. FIG.
As shown in FIG. 2, the fuel gas supply passage 22 and the fuel gas exhaust passage 24 are opposed to each other, and the oxidant gas supply passage 26 and the oxidant gas exhaust passage 28 are opposed to each other in a direction perpendicular to the fuel gas supply passage 22. The fuel gas and the oxidizing gas may be introduced into the fuel cell 2 at right angles from the respective flow passages.

【0033】[0033]

【発明の効果】本発明の燃料電池によれば、金属平板の
表裏面に、凹凸を有する金属薄板を設けてなる集電板を
固体電解質燃料電池間に設けたことにより、固体電解質
燃料電池を積層した場合、各平板型単電池が金属平板を
介して金属薄板により良好な接触を保った状態で電気的
に接続され、しかも平板型単電池が金属薄板により接触
されていることから燃料電池を運転させたときの温度変
動によってスタックの構成部材に膨張、収縮が生じて
も、その変動を吸収し平板型単電池の破損を防止でき
る。
According to the fuel cell of the present invention, a solid electrolyte fuel cell is provided by providing between the solid electrolyte fuel cells current collector plates provided with metal thin plates having irregularities on the front and back surfaces of a metal flat plate. When stacked, each flat cell is electrically connected to a thin metal plate via a metal flat plate while maintaining good contact.Moreover, since the flat cell is contacted by the thin metal plate, the fuel cell is Even if the components of the stack expand or contract due to temperature fluctuations during operation, the fluctuations can be absorbed to prevent damage to the flat cell.

【0034】また、金属平板を介してスペーサが積層さ
れることから、スペーサどうしを密着でき、ガスの通路
を完全に分離でき、漏洩等を確実に防止でき、また熱膨
張の差によるスタック等の破損を防止できる。
Further, since the spacers are laminated via the metal flat plate, the spacers can be adhered to each other, the gas passages can be completely separated, leakage can be reliably prevented, and the stack and the like due to the difference in thermal expansion can be prevented. Damage can be prevented.

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

【図1】本発明にかかる固体電解質燃料電池の一実施形
態を示す断面図である。
FIG. 1 is a cross-sectional view showing one embodiment of a solid oxide fuel cell according to the present invention.

【図2】金属薄板を示す斜視断面図である。FIG. 2 is a perspective sectional view showing a metal thin plate.

【図3】本発明にかかる固体電解質燃料電池の一実施形
態を示す分解斜視図である。
FIG. 3 is an exploded perspective view showing one embodiment of the solid oxide fuel cell according to the present invention.

【図4】金属薄板の他の例を示す図である。FIG. 4 is a view showing another example of a thin metal plate.

【図5】金属薄板の他の例を示す図である。FIG. 5 is a view showing another example of a metal thin plate.

【図6】金属薄板の他の例を示す図である。FIG. 6 is a diagram showing another example of a thin metal plate.

【図7】金属薄板の他の例を示す斜視図である。FIG. 7 is a perspective view showing another example of a thin metal plate.

【図8】金属薄板の他の例を示す斜視図である。FIG. 8 is a perspective view showing another example of a thin metal plate.

【図9】金属薄板の他の例を示す斜視図である。FIG. 9 is a perspective view showing another example of a thin metal plate.

【図10】金属薄板の他の例を示す断面図である。FIG. 10 is a cross-sectional view showing another example of a thin metal plate.

【図11】本発明にかかる固体電解質燃料電池の他の実
施形態を示す分解斜視図である。
FIG. 11 is an exploded perspective view showing another embodiment of the solid oxide fuel cell according to the present invention.

【図12】本発明にかかる固体電解質燃料電池の他の実
施形態を示す分解斜視図である。
FIG. 12 is an exploded perspective view showing another embodiment of the solid oxide fuel cell according to the present invention.

【図13】従来の固体電解質燃料電池を示す図である。FIG. 13 is a view showing a conventional solid oxide fuel cell.

【符号の説明】[Explanation of symbols]

2 燃料電池 3 集電板 4 固体電解質燃料電池 6 平板型単電池 8 第1スペーサ 10 第2スペーサ 11 金属薄板 12 金属平板 13 絞り部 14 収容部 16 保持薄板枠 17 接合材 18 突部 19 金属片 22 燃料ガス用供給通路 24 燃料ガス用排気通路 26 酸化剤ガス用供給通路 28 酸化剤ガス用排気通路 Reference Signs List 2 fuel cell 3 current collector 4 solid electrolyte fuel cell 6 flat unit cell 8 1st spacer 10 2nd spacer 11 metal thin plate 12 metal flat plate 13 squeezed portion 14 accommodation portion 16 holding thin plate frame 17 bonding material 18 protrusion 19 metal piece 22 Supply passage for fuel gas 24 Exhaust passage for fuel gas 26 Supply passage for oxidant gas 28 Exhaust passage for oxidant gas

───────────────────────────────────────────────────── フロントページの続き (72)発明者 伊東 健太郎 神奈川県横浜市磯子区汐見台3−3−3308 −310 Fターム(参考) 5H026 AA06 CC03 CC04 CC05 CC08 EE02  ────────────────────────────────────────────────── ─── Continued from the front page (72) Inventor Kentaro Ito 3-3-3308-310 F-term (reference) 5H026 AA06 CC03 CC04 CC05 CC08 EE02

Claims (12)

【特許請求の範囲】[Claims] 【請求項1】 積層された平板型単電池間に設けられ該
平板型単電池間の気体の流通を遮断する金属平板と、該
金属平板の表裏面に、該金属平板に接触した状態で設け
られ、かつ前記平板型単電池内に設けられた平板型単電
池の燃料極もしくは空気極に弾性をもって接触する金属
薄板とからなり、平板型単電池にかかる応力を緩和する
機能を備えたことを特徴とした固体電解質燃料電池の集
電板。
1. A metal flat plate provided between stacked flat type single cells to block the flow of gas between the flat type single cells, and provided on the front and back surfaces of the metal flat plate in contact with the metal flat plate. And a thin metal plate elastically contacting the fuel electrode or the air electrode of the flat cell provided in the flat cell, and having a function of relieving stress applied to the flat cell. A current collector plate for a solid electrolyte fuel cell.
【請求項2】 前記金属薄板は、表裏面の一方もしくは
双方に突部を有することを特徴とする請求項1に記載の
集電板。
2. The current collector plate according to claim 1, wherein the thin metal plate has a protrusion on one or both of the front and back surfaces.
【請求項3】 前記金属薄板の突部は、波状、矩形状、
ディンプル状、紡錘状、短冊状のいずれか、あるいはそ
れらの2以上の組み合わせであることを特徴とした請求
項2に記載の集電板。
3. The projection of the thin metal plate has a wavy shape, a rectangular shape,
The current collector plate according to claim 2, wherein the current collector plate is in any one of a dimple shape, a spindle shape, and a strip shape, or a combination of two or more thereof.
【請求項4】 平板型固体電解質の表裏面それぞれに燃
料極および空気極を対向して設けた平板型単電池を積層
して構成した燃料電池において、前記平板型単電池の間
に該平板型単電池間の気体の流通を遮断する金属平板を
配置し、凹凸を有する金属薄板を前記金属平板の表裏面
に、それぞれ該金属平板に接触した状態で取り付け、該
金属薄板に形成された凹凸によって該金属平板を挟む前
記平板型単電池を相互に電気的に接続させ、かつ該平板
型単電池にかかる応力を前記凹凸によって緩和させるこ
とを特徴とした固体電解質燃料電池の積層方法。
4. A fuel cell comprising a flat plate type cell in which a fuel electrode and an air electrode are provided opposite to each other on the front and back surfaces of a plate type solid electrolyte. A metal flat plate for blocking gas flow between the cells is arranged, and a thin metal plate having irregularities is attached to the front and back surfaces of the flat metal plate in a state of being in contact with the flat metal plate, respectively, by the unevenness formed on the thin metal plate. A method of laminating solid electrolyte fuel cells, characterized in that the flat plate cells sandwiching the flat metal plate are electrically connected to each other, and the stress applied to the flat plate cells is reduced by the unevenness.
【請求項5】 前記金属薄板の凹凸は、波状、矩形状、
ディンプル状、紡錘状、短冊状のいずれか、あるいはそ
れらの2以上の組み合わせであることを特徴とした請求
項4に記載の固体電解質燃料電池の積層方法。
5. The unevenness of the thin metal plate is wavy, rectangular,
5. The method for laminating a solid electrolyte fuel cell according to claim 4, wherein the method is a dimple shape, a spindle shape, a strip shape, or a combination of two or more thereof.
【請求項6】 平板型固体電解質の表裏面それぞれに燃
料極と空気極とを対向して設けた平板型単電池と、 積層した前記平板型単電池間に設けられ、該平板型単電
池間の気体の流通を遮断する金属平板と、 前記金属平板の表裏面にそれぞれ、該金属平板の表裏面
のそれぞれに接触した状態で設けられ、かつ前記平板型
単電池の燃料極もしくは空気極に弾性をもって接触する
突部を有し、積層された平板型単電池の空気極と燃料極
とを前記金属平板を介して導通させる金属薄板と、を備
えて構成したことを特徴とする固体電解質燃料電池。
6. A flat cell having a fuel electrode and an air electrode opposed to each other on the front and back surfaces of a flat solid electrolyte, and provided between the stacked flat cells and between the flat cells. A metal flat plate that blocks the flow of gas, and provided on the front and back surfaces of the metal flat plate, respectively, in contact with the front and back surfaces of the metal flat plate, and is elastic on the fuel electrode or air electrode of the flat plate cell. And a thin metal plate for conducting the air electrode and the fuel electrode of the laminated flat cell through the flat metal plate. .
【請求項7】 平板型固体電解質の表裏面それぞれに燃
料極と空気極とを対向して設けた平板型単電池と、 中央部に前記平板型単電池を収容する収容部を有し、か
つ周縁に前記収容部を挟み燃料ガス供給孔と燃料ガス排
気孔、及び酸化剤ガス供給孔と酸化剤ガス排気孔をそれ
ぞれ対向させて形成し、かつ前記燃料ガス供給孔および
燃料ガス排気孔を前記収容部に開口させた第1スペーサ
と、 少なくとも前記平板型単電池の空気極より大きい切り欠
きを中央に有し、周縁に前記燃料ガス供給孔、燃料ガス
排気孔、酸化剤ガス供給孔、酸化剤ガス排気孔をそれぞ
れ前記第1スペーサと同一に形成し、かつ酸化剤ガス供
給孔と酸化剤ガス排気孔を前記切り欠きに開口させた第
2スペーサと、 前記第2スペーサ上に積層され、該第2スペーサの前記
切り欠きを閉鎖する金属平板と、 前記金属平板の表裏面にそれぞれ設けられ、該金属平板
と前記平板型単電池の空気極、また該金属平板と該第2
スペーサ上に積層された次の平板型単電池の燃料極に接
する1組の金属薄板と、を備えたことを特徴とする固体
電解質燃料電池。
7. A flat cell having a fuel cell and an air electrode opposed to each other on the front and back surfaces of the flat solid electrolyte, a housing portion for housing the flat cell in a central portion, and A fuel gas supply hole and a fuel gas exhaust hole, and an oxidizing gas supply hole and an oxidizing gas exhaust hole are formed so as to face each other with the housing portion interposed therebetween, and the fuel gas supply hole and the fuel gas exhaust hole are formed so as to face each other. A first spacer having an opening in the housing portion, and a cutout larger than an air electrode of the flat plate type cell at the center, and a fuel gas supply hole, a fuel gas exhaust hole, an oxidant gas supply hole, A second spacer having an oxidizing gas supply hole and an oxidizing gas exhaust hole formed in the notch, each of which has the same agent gas exhaust hole as the first spacer, and is stacked on the second spacer; The cutting of the second spacer A metal flat plate for closing a notch; and a metal plate provided on the front and back surfaces of the metal flat plate, the metal flat plate and the air electrode of the flat plate type cell, and the metal flat plate and the second flat plate.
A solid electrolyte fuel cell, comprising: a set of thin metal plates that are in contact with the fuel electrode of the next flat plate cell stacked on the spacer.
【請求項8】 前記スペーサをアルミナフォーミングの
耐熱鋼としたことを特徴とする請求項7に記載の固体電
解質燃料電池。
8. The solid electrolyte fuel cell according to claim 7, wherein the spacer is made of heat resistant steel formed by alumina forming.
【請求項9】 前記平板型単電池の周囲に取り付けら
れ、該平板型単電池を前記第1スペーサ内に収容した際
該平板型単電池の周囲を閉塞する保持薄板枠を備えたこ
とを特徴とする請求項7または8に記載の固体電解質燃
料電池。
9. A holding thin plate frame attached to the periphery of the flat cell and closing the periphery of the flat cell when the flat cell is accommodated in the first spacer. The solid electrolyte fuel cell according to claim 7 or 8, wherein
【請求項10】 前記金属平板の周囲に絞りを形成し、
前記スペーサの内側に位置する絞りにより前記平板型単
電池の積層方向に対して直角な方向の応力も緩和するこ
とを特徴とする請求項7〜9のいずれか1項に記載の固
体電解質燃料電池。
10. An aperture is formed around the flat metal plate,
The solid electrolyte fuel cell according to any one of claims 7 to 9, wherein a stress located in a direction perpendicular to the laminating direction of the flat plate cells is also alleviated by an aperture located inside the spacer. .
【請求項11】 前記金属薄板は、表裏面の一方もしく
は双方に弾性を有する突部を備えたことを特徴とする請
求項6〜10のいずれか1項に記載の固体電解質燃料電
池。
11. The solid electrolyte fuel cell according to claim 6, wherein the thin metal plate has an elastic projection on one or both of the front and back surfaces.
【請求項12】 前記金属薄板の突部は、波状、矩形
状、ディンプル状、紡錘状、短冊状のいずれか、あるい
はそれらの2以上の組み合わせであることを特徴とした
請求項11に記載の固体電解質燃料電池。
12. The method according to claim 11, wherein the protrusion of the metal thin plate has any one of a wave shape, a rectangular shape, a dimple shape, a spindle shape, and a strip shape, or a combination of two or more thereof. Solid electrolyte fuel cell.
JP23828799A 1999-08-25 1999-08-25 Current collector plate and solid electrolyte fuel cell using the same Withdrawn JP2001068132A (en)

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