JP2004228050A - Cell stack and fuel battery - Google Patents

Cell stack and fuel battery Download PDF

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Publication number
JP2004228050A
JP2004228050A JP2003018010A JP2003018010A JP2004228050A JP 2004228050 A JP2004228050 A JP 2004228050A JP 2003018010 A JP2003018010 A JP 2003018010A JP 2003018010 A JP2003018010 A JP 2003018010A JP 2004228050 A JP2004228050 A JP 2004228050A
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Japan
Prior art keywords
current collecting
fuel cell
fuel
collecting member
cell stack
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JP2003018010A
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JP3898647B2 (en
Inventor
Noriaki Hamada
紀彰 浜田
Kenji Shimazu
健児 島津
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Kyocera Corp
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Kyocera Corp
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    • 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

Abstract

<P>PROBLEM TO BE SOLVED: To provide a cell stack and a fuel battery capable of improving current collector properties between fuel battery cells. <P>SOLUTION: On a cell stack 35, gas is made to flow through fuel battery cells 33, and a spiral current collector member 43, made of conductive member, electrically connecting the opposite fuel battery cells 33 to each other, is arranged between the fuel battery cells 33. <P>COPYRIGHT: (C)2004,JPO&NCIPI

Description

【0001】
【発明の属する技術分野】
本発明は、セルスタック及び燃料電池に関するもので、特に複数の燃料電池セルの集電特性が良好なセルスタック及び燃料電池に関するものである。
【0002】
【従来技術】
次世代エネルギーとして、近年、複数の燃料電池セルを収納容器内に収納した燃料電池が種々提案されている。
【0003】
従来の固体電解質型燃料電池は、複数の燃料電池セルを収納容器内に収納し、燃料電池セル同士を集電部材により電気的に直列又は並列に接続して構成されており、発電は燃料電池セルに酸素含有ガス及び燃料ガスを供給して600〜1000℃程度の高温で行われていた。
【0004】
そして、燃料電池セル間の電気的な接続を行う集電部材は、従来、繊維状の金属が集合した金属フェルト状のものが用いられている。このようなフェルト状の集電部材を用いた燃料電池は、複数の燃料電池セルを配列集合させ、例えば、一方の燃料電池セルのインターコネクタと、他方の燃料電池セルの外側電極との間に、フェルト状の集電部材を詰め込み燃料電池セルを直列に接続してセルスタックを形成し、このセルスタックを収納容器内に収納して構成されていた(特許文献1参照。)。
【0005】
【特許文献1】
特開2000−058088号公報
【0006】
【発明が解決しようとする課題】
しかしながら、上記した燃料電池では、フェルト状の集電部材は繊維状の金属から構成されているため、一方の燃料電池セルのインターコネクタと、他方の燃料電池セルの外側電極とは点接触となり、集電特性が未だ低いという問題があった。
【0007】
また、燃料電池セル間に集電部材を詰め込んだとしても、振動や集電部材の弾性低下等の原因で燃料電池セルとの接触が十分に行われなくなり、発電当初は集電特性はある程度良好であったとしても、集電特性が経時的に低下する可能性があった。
【0008】
さらに、燃料電池セル間に空気等の酸素含有ガスが導入されて発電する場合には、繊維状金属の表面から酸化が進行し、これにより集電特性が低下し、また金属フェルトの弾性力が低下し、経時的に集電特性が低下するという問題もあった。
【0009】
また、一方の燃料電池セルのインターコネクタと他方の燃料電池セルの外側電極との間に集電部材を詰め込む際に、集電部材がフェルト状であることに起因して、一方の燃料電池セルと他方の燃料電池セルの外側電極同士が導通してしまうという危険性もあった。
【0010】
本発明は、燃料電池セル間の集電特性を向上できるセルスタック及び燃料電池を提供することを目的とする。
【0011】
【課題を解決するための手段】
本発明のセルスタックは、燃料電池セル間をガスが流通するセルスタックであって、前記燃料電池セル間に、線状部材を螺旋状に巻回してなる螺旋状集電部材を配置し、対向する前記燃料電池セル同士を電気的に接続してなることを特徴とする。
【0012】
このような螺旋状集電部材の線の断面は円でも、楕円でもよく、また例えば、四角状であってもよいが、螺旋状集電部材が変形したとしても楕円状であれば、燃料電池セルとの接触面積を大きくすることができるため、線の断面は楕円であることが望ましい。
【0013】
このようなセルスタックでは、集電部材が螺旋形状であり、その両端部が対向する燃料電池セルの外面にそれぞれ当接しており、例えば、上記のように、螺旋状集電部材の線の断面が例えば、楕円である場合には、燃料電池セルの外面と面接触し、従来のようなフェルト状の集電部材よりも燃料電池セルに当接する面積が大きくなり、集電特性を向上できる。
【0014】
また、螺旋状集電部材が燃料電池セル間方向および螺旋進行方向にバネ性を有するため弾性力も大きく、振動等が生じたとしても燃料電池セルとの十分な接触を長期間確保できる。さらに、螺旋状集電部材は、フェルト状集電部材よりも線径が太いため、収納容器内が高温となった場合でも、従来のフェルト状の集電部材よりも焼結しにくく、そのため、弾性を失うことがなく、燃料電池セルとの十分な接触を長期間確保できる。
【0015】
また、本発明のセルスタックは、螺旋状集電部材が、螺旋進行方向から見て鼓形状であり、螺旋状集電部材の略平坦部が燃料電池セルと当接してなることを特徴とする。このように螺旋状集電部材の形状を鼓形状とし、屈曲部を螺旋状集電部材の略平坦部間に形成することで、燃料電池セル間の距離が小さくなったとしても、螺旋状集電部材の幅が広がることがないため、他の燃料電池セルと接触し電気的に短絡することを防止できる。
【0016】
また、本発明のセルスタックは、螺旋状集電部材がガス流通方向に向けて螺旋状に形成されていることを特徴とする。このように、ガス流通方向と集電部材の螺旋の進行方向を一致させることで、燃料電池セル間に配置された螺旋状集電部材の螺旋の内部にガスが流通可能な空間が形成され、燃料電池セルへのガス供給を容易にすることができる。
【0017】
また、本発明のセルスタックは、螺旋状集電部材の燃料電池セル外面との当接部には凹凸が形成されていることを特徴とする。このようなセルスタックでは、凹凸が形成されている螺旋状集電部材の当接部が、対向する燃料電池セルの外面に当接することになるが、燃料電池セル外面には螺旋状集電部材の当接部の凸部が当接し、燃料電池セル外面と当接部の凸部間との間には空間が形成されており、この空間をガスが通過することになるため、ガスの外側電極表面への供給を増加して、多孔質な外側電極を介して固体電解質まで供給されるガス量を増加でき、発電性能を向上できる。
【0018】
また、本発明のセルスタックは、螺旋状集電部材の燃料電池セル外面との当接部に波形の凹凸が形成されており、前記螺旋状集電部材の当接部に形成された凹部がガス流通方向に形成されていることを特徴とする。この場合には、ガスは螺旋状集電部材の当接部に形成された凹部と外側電極外面との間を通過し、ガスの外側電極表面への供給を増加でき、発電性能を向上できる。
【0019】
さらに、本発明のセルスタックでは、燃料電池セルは、軸長方向にガス流路が形成された支持体の表面に、内側電極、固体電解質、外側電極を順次形成し、前記固体電解質及び前記外側電極が形成されていない支持体又にインターコネクタを設けてなり、一方の燃料電池セルのインターコネクタと他方の燃料電池セルの外側電極に、螺旋状集電部材が当接していることを特徴とする。このように燃料電池セルを電気的に直列に接続する場合に好適に用いられる。
【0020】
また、本発明のセルスタックでは、燃料電池セルは、酸素含有ガスに曝される外側電極を有しており、螺旋状集電部材が、導電性を有する金属又は合金の表面を耐酸化性物質で被覆して構成されていることを特徴とする。螺旋状集電部材が耐酸化性を有するため、螺旋状集電部材が酸素含有ガスに曝されたとしても良好な電気伝導性を有することができる。
【0021】
さらに、本発明のセルスタックでは、螺旋状集電部材の燃料電池セル外面との当接部は、導電性ペーストにより対向する燃料電池セルの外面に接合されていることを特徴とする。これにより、螺旋状集電部材と燃料電池セル間の電気的接続を確実に行うことができる。例えば、螺旋状集電部材の両端部に凹凸が形成されている場合には、凸部が導電性ペーストにより燃料電池セルの外面に接合されることになる。
【0022】
また、本発明のセルスタックでは、燃料電池セルは扁平状であり、対向する燃料電池セルの外面は略平坦であることを特徴とする。このように、対向する燃料電池セルの外面が略平坦である場合には、螺旋状集電部材が燃料電池セル外面の平坦部に確実に当接するため、集電特性を向上できる。
【0023】
本発明の燃料電池は、収納容器内に、上記したセルスタックを収納してなることを特徴とする。このような燃料電池では、セルスタックが良好な集電特性を有するため、優れた発電特性を発揮できる。
【0024】
【発明の実施の形態】
図1は、本発明の燃料電池の一形態を示すもので、符号31は断熱構造を有する収納容器を示している。この収納容器31の内部には、複数の燃料電池セル33が集合したセルスタック35と、セルスタック35の上方に形成された燃焼空間37と、この燃焼空間37を挿通する酸素含有ガス供給管39と、燃焼空間37の上方に設けられた熱交換部41とが設けられている。
【0025】
収納容器31は、耐熱性金属からなる枠体31aと、この枠体31aの内面に設けられた断熱材31bとから構成されている。セルスタック35の下方には、燃料ガスを燃料電池セル33に供給するための燃料ガスタンク45が設けられ、この燃料ガスタンク45には、外部から燃料ガスを燃料ガスタンク45に供給するための燃料ガス供給管51が接続されている。
【0026】
燃料ガスタンク45には、燃料電池セル33の下端部に取り付けられた取付治具53が螺着しており、これにより、燃料電池セル33が燃料ガスタンク45にそれぞれ立設している。即ち、取付治具53は、燃料電池セル33の端部に取り付けられたセル端部側取付治具53aと、両端部がセル端部側取付治具53a及び燃料ガスタンク45にそれぞれ螺着する連結部材53bとから構成されており、連結部材53bの両端部には向きが逆のねじ部が形成され、連結部材53bを一方側に回転させると、両端部がセル端部側取付治具53a及び燃料ガスタンク45にそれぞれ螺着するように形成されている。
【0027】
セル端部側取付治具53a、連結部材53bには、燃料ガスタンク45と燃料電池セル33の燃料ガス流路に連通するように貫通孔が形成されている。
【0028】
また、燃焼空間37を挿通する酸素含有ガス供給管39は、その先端部が燃料電池セル33間に位置している。この酸素含有ガス供給管39から供給される酸素含有ガスは、燃料ガスタンク45側に向けて噴出した後、熱交換部41側に流れることになる。従って、発電で用いられなかった余剰の酸素含有ガスは、燃料電池セル33間を通って燃料電池セル33の上方に流れ、発電で用いられなかった余剰の燃料ガスは、燃料電池セル33の燃料ガス流路を通って燃料電池セル33の上方から吹き出し、燃料電池セル33の上端近傍において、燃料ガスと酸素含有ガスが反応して燃焼するように構成されている。
【0029】
熱交換部41は、熱交換器41aと、燃焼空間37を介してセルスタック35に対向して設けられた酸素含有ガス収容室41bとから構成されている。
【0030】
熱交換器41aは、例えば、プレートフィン型構造とされている。燃焼ガスは、一点鎖線で示したように熱交換器41aの下部側面から導入され、熱交換器41aの上方へ排出され、一方、酸素含有ガスは、図1に破線で示したように熱交換器41aの上部側面から導入され、熱交換器41aの下方へ導かれ、酸素含有ガス収容室41b内に導入される。
【0031】
酸素含有ガス収容室41bは、熱交換器41aのセルスタック35側端面に設けられており、熱交換器41aを通過した酸素含有ガスが一旦収容されるようになっている。また、酸素含有ガス収容室41bには、複数の酸素含有ガス供給管39の一端が開口し、連通している。
【0032】
また、酸素含有ガス収容室41bの側面と断熱材31bとの間、即ち酸素含有ガス収容室41bの周囲は、燃焼空間37中の燃焼ガスを熱交換器41aに導入する燃焼ガス導入口71とされている。この燃焼ガス導入口71を介して燃焼ガスが熱交換器41aへ導出される。
【0033】
収納容器31内のセルスタック35は、図2に示すように、燃料電池セル33を3列に整列して構成されており、隣設した2列の最外部の燃料電池セル33の電極同士が導電部材42で接続され、これにより3列に整列した複数の燃料電池セル33が電気的に直列に接続している。尚、図1では4列として記載している。
【0034】
本発明の燃料電池セル33は、図2に示したように、断面が扁平状で、全体的に見て板状、もしくは楕円柱状であり、その内部には複数の燃料ガス流路34が形成されている。
【0035】
この燃料電池セル33は、断面が扁平状で、全体的に見て板状、もしくは楕円柱状の多孔質な支持体33aの外面に、多孔質な燃料側電極33b、緻密質な固体電解質33c、多孔質な導電性セラミックスからなる酸素側電極33dを順次積層し、酸素側電極33dと反対側の支持体33aの外面にインターコネクタ33eを形成して構成されている。
【0036】
即ち、燃料電池セル33は、断面形状が、幅方向両端に設けられた弧状部と、これらの弧状部を連結する一対の平坦部とから構成されており、一対の平坦部は平坦であり、ほぼ平行に形成されている。これらの一対の平坦部のうち、一方にはインターコネクタ33eが形成され、他方の平坦部には燃料側電極33b、固体電解質33c、酸素側電極33dが順次形成されて構成されている。
【0037】
そして、本発明のセルスタックでは、一方の燃料電池セル33と他方の燃料電池セル33との間に螺旋状集電部材43が配置され、一方の燃料電池セル33の燃料側電極33bは、支持体33aに設けられたインターコネクタ33e、螺旋状集電部材43を介して他方の燃料電池セル33の酸素側電極33dに電気的に接続されている。
【0038】
螺旋状集電部材43は、ガス流通方向から見て円形状であり、図3(a)、(b)に示すようにガス流通方向から見て螺旋状に形成され、燃料電池セル33間に配置されている。螺旋状集電部材43を形成する線状導電部材の断面は円状、楕円状、角状とされており、特に、燃料電池セル33との当接面積を増加させるためには楕円状、あるいは角状が望ましい。
【0039】
このような螺旋状集電部材43は、図3(a)、(b)に示すように、螺旋の進行方向から見た形状は例えば、楕円状となる。この楕円は燃料電池セル33に当接する略平面の43aと、燃料電池セル33間の電気的接続と物理的接続とを保つ非当接部43bとから形成される。
【0040】
このような螺旋状集電部材43は、燃料電池セル33間方向及び燃料電池セル33の軸長方向への弾性を有しているため、温度変化による燃料電池セル33間の距離の変化や、燃料電池セル33の軸長方向の長さの変化にも柔軟に追随することが可能で、発電、停止に伴う熱サイクルを繰り返しても燃料電池セル33間の電気的接続を保つことができる。また、同様の理由により、振動などによる断線が起こることもない。
【0041】
また、螺旋状集電部材43の螺旋進行方向から見た形状は円状としているが、燃料電池セル33間の距離が縮まった場合でも、螺旋状集電部材43の変形により隣り合う螺旋状集電部材43と接触するおそれがなく、また、他の燃料電池セル33と接触するおそれがないことから、図3(c)、(d)に示すように螺旋状集電部材43の螺旋進行方向から見た形状は鼓形状であることが望ましい。
【0042】
この鼓状の螺旋状集電部材43は、燃料電池セル33に当接する略平面の43aと、燃料電池セル33間の電気的接続と物理的接続とを保つ非当接部43bに形成された屈曲部43cとから形成される。
【0043】
この屈曲部43cは燃料電池セル33間方向の弾性を生じるとともに、燃料電池セル33間の距離が小さくなった場合には屈曲部43cが螺旋状集電部材43の内側に移動するため、例えば、隣り合う螺旋状集電部材43や隣り合う燃料電池セル33と干渉したり、接触することがなく、電気的接続の信頼性を向上させることができる。
【0044】
図4に示すように螺旋状集電部材43の当接部43aには波形の凹凸が形成されており、当接部43aに形成された凹部43a1がガス流通方向に形成されている。図4では、紙面に向かって垂直方向がガス流通方向となる。ガスは、螺旋状集電部材43の当接部43aに形成された凹部43a1と酸素側電極33d外面との間を通過し、酸素含有ガスの酸素側電極33d表面への供給を増加でき、発電性能を向上できる。
【0045】
また、螺旋状集電部材43は、対向する燃料電池セル33間に複数配置されている。複数配置することにより、燃料電池セル33間の集電抵抗を低下させることができ、燃料電池セル33間の集電特性を向上できる。
【0046】
また、螺旋状集電部材43は、対向する燃料電池セル33の平坦部であるインターコネクタ33eと、酸素側電極33dとの間に配置され、燃料電池セル33同士が直列に接続されており、燃料電池セル33の平坦部に螺旋状集電部材43の当接部43aが当接しているため、確実に当接し、電気的接続を確実に行うことができる。
【0047】
また、当接部43aの燃料電池セル33側に突出した部分が、導電ペースト44、例えば、Agペーストを介在して燃料電池セル33の酸素側電極33dやインターコネクタ33eに接合されている。このAgペーストは例えば、発電時に焼き付けられ、当接部43aが、燃料電池セル33のインターコネクタ33eと酸素側電極33dに接合し、これにより、螺旋状集電部材43と燃料電池セル33との電気的接続を十分にとることができる。
【0048】
尚、当接部43aは全面がインターコネクタ33eに当接し、酸素側電極33dには、上記したように、当接部43aの酸素側電極33d側に突出した部分を当接させても良い。この場合には、当接部43aの接続固定をさらに確実に行うことができる。
【0049】
これらの螺旋状集電部材43は、対向する燃料電池セル33間に複数介在されており、これらの螺旋状集電部材43は、導電性を有するCr、Feを主成分とするフェライト系ステンレスの表面をAgからなる耐酸化性物質で被覆して構成されている。尚、螺旋状集電部材43は導電性を有する金属又は合金を主成分とするものの表面を耐酸化性物質で被覆したものであれば、上記したものに限定されるものではない。
【0050】
そして、本発明の燃料電池では、螺旋状集電部材43がバネ性を有し、例えば、断面が楕円状、あるいは角状の当接部43aが燃料電池セル33の外面と面接触するため、従来のようなフェルト状の集電部材よりも燃料電池セル33に当接する面積が大きくなり、集電特性を向上できる。また、螺旋状集電部材43は弾性力も大きく、振動等が生じたとしても燃料電池セル33との十分な接触を長期間確保できる。また、特に、当接部43aに凹凸を形成し、螺旋状集電部材43と燃料電池セル33外面との間を燃料ガスが通過することにより、燃料ガスを固体電解質33bへ十分に供給でき、発電特性を向上できる。
【0051】
さらに、螺旋状集電部材43は線状であるため、収納容器31内が高温となった場合でも、従来のフェルト状の集電部材よりも焼結しにくく、また、燃料電池セル33との十分な接触を長期間確保できる。
【0052】
以上のように構成された燃料電池では、外部からの酸素含有ガス(例えば空気)を、酸素含有ガス管73を介して熱交換器41aに導入し、酸素含有ガス収容室41bに導入し、酸素含有ガス供給管39を介して燃料電池セル33間に噴出させるとともに、燃料ガス(例えば水素)を燃料ガス供給管51を介して燃料電池セル33の燃料ガス流路に供給し発電させる。
【0053】
発電に用いられなかった余剰の燃料ガスは燃料ガス流路の上端から燃焼空間37内に噴出し、発電に用いれらなかった余剰の酸素含有ガスは燃焼空間37内に流れ、余剰の燃料ガスと余剰の酸素含有ガスを反応させて燃焼させ、燃焼ガスを発生させ、この燃焼ガスが燃焼ガス導入口71を介して熱交換器41aに導出され、熱交換器41aの上端から排出される。
【0054】
また、発電に寄与しなかった余剰の燃料ガスと酸素含有ガスが燃焼空間37内に導入され、この燃焼空間37中で反応して燃焼し、この燃焼ガス及び外部の酸素含有ガスを熱交換器41aに導入し、この熱交換器41aで燃焼ガスと酸素含有ガスとの間で熱交換させ、起動時に酸素含有ガスを予熱することができ、また、酸素含有ガス供給管39が燃焼空間37を挿通することにより、燃焼ガスにより酸素含有ガス供給管39内の酸素含有ガスをさらに加熱することができるため、加熱した酸素含有ガスにより燃料電池セル33を間接的に加熱して実質的に発電するまでの起動時間を短縮できる。
【0055】
さらに、セルスタック35の上部に燃焼空間37、酸素含有ガス収容室41b、熱交換器41aが隣接して形成されているため、燃焼空間37で燃焼した高温の燃焼ガスを、配管等を用いることなく熱交換器41aに直接導入でき、簡単な構造で酸素含有ガスの予熱効率を大きくできる。
【0056】
また、収納容器31内で、燃焼ガスと酸素含有ガスとを熱交換できるため、酸素含有ガスの予熱を行うためのバーナーを収納容器31内に別途設ける必要がなく、小型にでき、しかも燃焼ガスを有効利用できる。
【0057】
さらに、熱交換器41aに酸素含有ガス収容室41bを設けたので、熱交換器41aと酸素含有ガス供給管39との接続を酸素含有ガス収容室41bを介して行うことができ、熱交換器41aからの酸素含有ガスを発電空間75内に確実に供給できる。
【0058】
尚、本発明は上記形態に限定されるものではなく、発明の要旨を変更しない範囲で種々の変更が可能である。例えば、上記形態では、図2に示したような扁平状で複数の燃料ガス流路34を有する燃料電池セル33を用いて説明したが、燃料電池セル33は燃料ガス流路34が一つであっても良く、燃料電池セル33の形状は特に限定されるものではない。
【0059】
また、螺旋状集電部材43は燃料電池セル33間に複数配置される場合もあるが、この場合、例えば、それぞれの螺旋状集電部材43を結合させ、例えば、イカダ状の形状とすることで、螺旋状集電部材43の配置が容易となる。
【0060】
また、さらに、上記例では、燃料電池セル33を直列に接続した例について説明したが、このような螺旋状集電部材43が複数結合した幅広の螺旋状集電部材43を用いて、燃料電池セル33を複数、並列に接続することで組み立てが容易となる。
【0061】
また、燃料側電極33bを内側電極としたが、酸素側電極33dを内側電極としても良い。
【0062】
さらに、一つの燃料ガスタンク45を用いて燃料電池セル33に燃料ガスを供給する場合について説明したが、本発明では、燃料電池セル33列毎に燃料ガスタンク45を設け、これらの間に、燃料電池セル33を直接加熱するバーナを設けることもできる。この場合には、起動時にバーナにより燃料電池セル33を直接加熱し、さらに起動を迅速に行うことができる。
【0063】
【発明の効果】
本発明のセルスタックでは、集電部材が螺旋状であり、対向する燃料電池セルの外面に当接しており、螺旋状集電部材がバネ性を有するため、燃料電池セルの外面と面接触し、集電特性を向上できるとともに、集電部材は螺旋状であるため弾性力も大きく、燃料電池セルとの十分な接触を長期間確保でき、さらに、集電部材は例えば、線状であるため焼結しにくく、燃料電池セルとの十分な接触を長期間確保できる。
【図面の簡単な説明】
【図1】本発明の燃料電池を示す説明図である。
【図2】図1のセルスタックを示す横断面図である。
【図3】螺旋状集電部材を用いて燃料電池セルを接続した状態と、螺旋状集電部材の形状を示すもので、(a)は螺旋状集電部材を側方からみた側面図、(b)は(a)で用いた螺旋状集電部材をガス流通方向から見た平面図、(c)は他の形態の螺旋状集電部材を側方からみた側面図、(d)は(c)で用いた螺旋状集電部材をガス流通方向から見た平面図である。
【図4】燃料電池セルと螺旋状集電部材との接続構造を示す説明図である。
【符号の説明】
31・・・収納容器
33・・・燃料電池セル
33a・・・支持体
33b・・・燃料側電極(内側電極)
33c・・・固体電解質
33d・・・酸素側電極(外側電極)
33e・・・インターコネクタ
34・・・ガス流路
35・・・セルスタック
43・・・螺旋状集電部材
43a・・・当接部(両端部)
43a1・・・当接部の凹部
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a cell stack and a fuel cell, and more particularly to a cell stack and a fuel cell having a plurality of fuel cells having good current collection characteristics.
[0002]
[Prior art]
In recent years, various fuel cells in which a plurality of fuel cells are stored in a storage container have been proposed as next-generation energy.
[0003]
A conventional solid oxide fuel cell has a structure in which a plurality of fuel cells are housed in a housing, and the fuel cells are electrically connected in series or in parallel by a current collecting member. Oxygen-containing gas and fuel gas have been supplied to the cell, and have been performed at a high temperature of about 600 to 1000 ° C.
[0004]
As a current collecting member for making electrical connection between fuel cells, a metal felt-like member in which fibrous metals are gathered is conventionally used. A fuel cell using such a felt-shaped current collecting member has a plurality of fuel cells arranged in an array, for example, between an interconnector of one fuel cell and an outer electrode of the other fuel cell. A fuel cell is packed in series with a felt-shaped current collecting member to form a cell stack, and the cell stack is stored in a storage container (see Patent Document 1).
[0005]
[Patent Document 1]
JP 2000-058088 A
[Problems to be solved by the invention]
However, in the above-described fuel cell, since the felt-shaped current collecting member is formed of a fibrous metal, the interconnector of one fuel cell and the outer electrode of the other fuel cell are in point contact, There was a problem that the current collecting characteristics were still low.
[0007]
Also, even if the current collecting member is packed between the fuel cells, the contact with the fuel cell is not sufficiently performed due to vibration or a decrease in the elasticity of the current collecting member, and the current collecting characteristics are somewhat good at the beginning of power generation. However, the current collecting characteristics may deteriorate over time.
[0008]
Furthermore, when power is generated by introducing an oxygen-containing gas such as air between the fuel cells, oxidation proceeds from the surface of the fibrous metal, thereby deteriorating the current collection characteristics and reducing the elastic force of the metal felt. There is also a problem that the current collection characteristics decrease over time.
[0009]
Further, when the current collecting member is packed between the interconnector of one fuel cell and the outer electrode of the other fuel cell, one of the fuel cells is There is also a danger that the outer electrodes of the other fuel cells will conduct.
[0010]
An object of the present invention is to provide a cell stack and a fuel cell that can improve current collection characteristics between fuel cells.
[0011]
[Means for Solving the Problems]
The cell stack of the present invention is a cell stack in which gas flows between fuel cells, wherein a spiral current collecting member formed by spirally winding a linear member is arranged between the fuel cells, and is opposed to each other. The fuel cells are electrically connected to each other.
[0012]
The cross section of the line of such a spiral current collecting member may be a circle or an ellipse, and may be, for example, a quadrangle. The cross section of the line is desirably elliptical so that the contact area with the cell can be increased.
[0013]
In such a cell stack, the current collecting member has a spiral shape, and both ends of the current collecting member are in contact with the outer surfaces of the fuel cells facing each other. For example, as described above, the cross section of the line of the spiral current collecting member For example, when the shape is elliptical, the area in contact with the outer surface of the fuel cell unit and the area in contact with the fuel cell unit becomes larger than that of a conventional felt-shaped current collecting member, so that the current collecting characteristics can be improved.
[0014]
Further, since the spiral current collecting member has a spring property in the direction between the fuel cells and in the spiral traveling direction, the elastic force is large, and even if vibration or the like occurs, sufficient contact with the fuel cell can be ensured for a long time. Furthermore, since the spiral current collecting member has a larger wire diameter than the felt current collecting member, even when the temperature inside the storage container becomes high, the spiral current collecting member is less likely to be sintered than the conventional felt current collecting member. Sufficient contact with the fuel cell can be ensured for a long time without losing elasticity.
[0015]
Further, the cell stack of the present invention is characterized in that the spiral current collecting member has a drum shape when viewed from the spiral traveling direction, and a substantially flat portion of the spiral current collecting member is in contact with the fuel cell. . By forming the spiral current collecting member into a drum shape and forming the bent portion between substantially flat portions of the spiral current collecting member in this manner, even if the distance between the fuel cells is reduced, the spiral current collecting member becomes smaller. Since the width of the electric member does not increase, it is possible to prevent the electric member from being in contact with another fuel cell and being electrically short-circuited.
[0016]
Further, the cell stack of the present invention is characterized in that the spiral current collecting member is spirally formed in the gas flowing direction. In this way, by matching the gas flow direction and the spiral traveling direction of the current collecting member, a space through which gas can flow is formed inside the spiral of the spiral current collecting member disposed between the fuel cells, Gas supply to the fuel cell unit can be facilitated.
[0017]
Further, the cell stack of the present invention is characterized in that irregularities are formed at a contact portion of the spiral current collector with the outer surface of the fuel cell. In such a cell stack, the contact portion of the spiral current collecting member having the unevenness abuts on the outer surface of the opposed fuel cell, but the spiral current collecting member is formed on the outer surface of the fuel cell. The convex portion of the abutting portion abuts, and a space is formed between the outer surface of the fuel cell and the convex portion of the abutting portion, and the gas passes through this space. By increasing the supply to the electrode surface, the amount of gas supplied to the solid electrolyte via the porous outer electrode can be increased, and the power generation performance can be improved.
[0018]
Further, in the cell stack of the present invention, corrugated unevenness is formed in a contact portion of the spiral current collecting member with the outer surface of the fuel cell, and a concave portion formed in the contact portion of the spiral current collecting member is formed. It is characterized in that it is formed in the gas flow direction. In this case, the gas passes between the concave portion formed in the contact portion of the spiral current collector and the outer surface of the outer electrode, so that the supply of gas to the outer electrode surface can be increased, and the power generation performance can be improved.
[0019]
Further, in the cell stack of the present invention, the fuel cell includes an inner electrode, a solid electrolyte, and an outer electrode sequentially formed on the surface of the support having the gas flow path formed in the axial direction, and the solid electrolyte and the outer electrode are formed. An interconnector is provided on a support or an electrode on which no electrode is formed, and a spiral current collecting member is in contact with the interconnector of one fuel cell and the outer electrode of the other fuel cell. I do. Thus, it is suitably used when the fuel cells are electrically connected in series.
[0020]
Further, in the cell stack of the present invention, the fuel cell has the outer electrode exposed to the oxygen-containing gas, and the spiral current collecting member has a conductive metal or alloy formed on the surface of the oxidation-resistant substance. It is characterized by being constituted by being coated with. Since the spiral current collecting member has oxidation resistance, even if the spiral current collecting member is exposed to an oxygen-containing gas, it can have good electric conductivity.
[0021]
Furthermore, the cell stack of the present invention is characterized in that the contact portion of the spiral current collector with the outer surface of the fuel cell is joined to the outer surface of the fuel cell opposed by a conductive paste. Thereby, electrical connection between the spiral current collector and the fuel cell unit can be reliably performed. For example, when unevenness is formed at both ends of the spiral current collecting member, the projecting portion is joined to the outer surface of the fuel cell by the conductive paste.
[0022]
Further, in the cell stack of the present invention, the fuel cells are flat, and the outer surfaces of the opposed fuel cells are substantially flat. As described above, when the outer surfaces of the opposed fuel cells are substantially flat, the spiral current collecting member surely comes into contact with the flat portion of the outer surface of the fuel cells, so that the current collecting characteristics can be improved.
[0023]
The fuel cell of the present invention is characterized in that the above-described cell stack is stored in a storage container. In such a fuel cell, since the cell stack has good current collecting characteristics, excellent power generation characteristics can be exhibited.
[0024]
BEST MODE FOR CARRYING OUT THE INVENTION
FIG. 1 shows an embodiment of the fuel cell of the present invention, and reference numeral 31 denotes a storage container having a heat insulating structure. Inside the storage container 31, a cell stack 35 in which a plurality of fuel cells 33 are assembled, a combustion space 37 formed above the cell stack 35, and an oxygen-containing gas supply pipe 39 passing through the combustion space 37. And a heat exchange section 41 provided above the combustion space 37.
[0025]
The storage container 31 includes a frame 31a made of a heat-resistant metal and a heat insulating material 31b provided on an inner surface of the frame 31a. A fuel gas tank 45 for supplying fuel gas to the fuel cell 33 is provided below the cell stack 35. The fuel gas tank 45 is provided with a fuel gas supply for supplying fuel gas to the fuel gas tank 45 from outside. Tube 51 is connected.
[0026]
An attachment jig 53 attached to the lower end of the fuel cell 33 is screwed to the fuel gas tank 45, whereby the fuel cells 33 stand on the fuel gas tank 45, respectively. That is, the attachment jig 53 is connected to the cell end side attachment jig 53 a attached to the end of the fuel cell 33 and both ends are screwed to the cell end side attachment jig 53 a and the fuel gas tank 45, respectively. The connecting member 53b is formed with screw portions having opposite directions at both ends, and when the connecting member 53b is rotated to one side, the both ends are connected to the cell end side mounting jig 53a and The fuel gas tanks 45 are formed so as to be screwed respectively.
[0027]
A through hole is formed in the cell end side mounting jig 53 a and the connecting member 53 b so as to communicate with the fuel gas tank 45 and the fuel gas flow path of the fuel cell 33.
[0028]
The oxygen-containing gas supply pipe 39 passing through the combustion space 37 has a tip located between the fuel cells 33. The oxygen-containing gas supplied from the oxygen-containing gas supply pipe 39 is ejected toward the fuel gas tank 45, and then flows toward the heat exchange unit 41. Therefore, the excess oxygen-containing gas not used in the power generation flows above the fuel cells 33 between the fuel cells 33, and the excess fuel gas not used in the power generation is The fuel gas is blown from above the fuel cell 33 through the gas flow path, and the fuel gas and the oxygen-containing gas react and burn near the upper end of the fuel cell 33.
[0029]
The heat exchange section 41 includes a heat exchanger 41a and an oxygen-containing gas storage chamber 41b provided to face the cell stack 35 via the combustion space 37.
[0030]
The heat exchanger 41a has, for example, a plate fin structure. The combustion gas is introduced from the lower side surface of the heat exchanger 41a as shown by a dashed line and discharged above the heat exchanger 41a, while the oxygen-containing gas is subjected to heat exchange as shown by a broken line in FIG. It is introduced from the upper side surface of the vessel 41a, is guided below the heat exchanger 41a, and is introduced into the oxygen-containing gas storage chamber 41b.
[0031]
The oxygen-containing gas storage chamber 41b is provided on the end face of the heat exchanger 41a on the cell stack 35 side, and temporarily stores the oxygen-containing gas that has passed through the heat exchanger 41a. One end of a plurality of oxygen-containing gas supply pipes 39 is open and communicates with the oxygen-containing gas storage chamber 41b.
[0032]
Further, between the side surface of the oxygen-containing gas storage chamber 41b and the heat insulating material 31b, that is, around the oxygen-containing gas storage chamber 41b, a combustion gas inlet 71 for introducing the combustion gas in the combustion space 37 to the heat exchanger 41a is provided. Have been. The combustion gas is led out to the heat exchanger 41a via the combustion gas inlet 71.
[0033]
As shown in FIG. 2, the cell stack 35 in the storage container 31 is configured by arranging the fuel cells 33 in three rows, and the electrodes of the two outermost fuel cells 33 adjacent to each other are connected to each other. The plurality of fuel cells 33 arranged in three rows are electrically connected in series by being connected by the conductive member 42. Note that FIG. 1 shows four columns.
[0034]
As shown in FIG. 2, the fuel cell 33 of the present invention has a flat cross section, a plate shape or an elliptic column shape as a whole, and a plurality of fuel gas flow paths 34 formed therein. Have been.
[0035]
The fuel cell 33 has a flat cross section, and has a plate-like or elliptic columnar porous support 33a as a whole, and a porous fuel-side electrode 33b, a dense solid electrolyte 33c, An oxygen-side electrode 33d made of porous conductive ceramics is sequentially laminated, and an interconnector 33e is formed on an outer surface of a support 33a opposite to the oxygen-side electrode 33d.
[0036]
That is, the fuel cell 33 has a cross-sectional shape including arc-shaped portions provided at both ends in the width direction and a pair of flat portions connecting these arc-shaped portions, and the pair of flat portions is flat, They are formed almost in parallel. An interconnector 33e is formed on one of the pair of flat portions, and a fuel-side electrode 33b, a solid electrolyte 33c, and an oxygen-side electrode 33d are sequentially formed on the other flat portion.
[0037]
In the cell stack of the present invention, the spiral current collecting member 43 is disposed between the one fuel cell 33 and the other fuel cell 33, and the fuel electrode 33b of the one fuel cell 33 is supported. It is electrically connected to an oxygen-side electrode 33d of the other fuel cell 33 via an interconnector 33e provided on the body 33a and a spiral current collecting member 43.
[0038]
The spiral current collecting member 43 has a circular shape when viewed from the gas flow direction, and is formed in a spiral shape when viewed from the gas flow direction as shown in FIGS. Are located. The cross section of the linear conductive member forming the spiral current collecting member 43 is circular, elliptical, or angular. In particular, in order to increase the contact area with the fuel cell 33, the cross section is elliptical, or A square shape is desirable.
[0039]
As shown in FIGS. 3A and 3B, such a spiral current collecting member 43 has, for example, an elliptical shape when viewed in the spiral traveling direction. The ellipse is formed by a substantially flat surface 43a that comes into contact with the fuel cells 33, and a non-contact portion 43b that maintains electrical and physical connections between the fuel cells 33.
[0040]
Since such a spiral current collecting member 43 has elasticity in the direction between the fuel cells 33 and in the axial direction of the fuel cells 33, a change in the distance between the fuel cells 33 due to a temperature change, It is possible to flexibly follow a change in the length of the fuel cell 33 in the axial direction, and the electrical connection between the fuel cells 33 can be maintained even when a heat cycle accompanying power generation and stop is repeated. For the same reason, disconnection due to vibration or the like does not occur.
[0041]
The spiral current collecting member 43 has a circular shape when viewed from the spiral traveling direction. However, even when the distance between the fuel cells 33 is reduced, the spiral current collecting member 43 is deformed to form a spiral current collecting member 43 that is adjacent to the spiral current collecting member 43. Since there is no risk of contact with the current collecting member 43 and no risk of contact with other fuel cells 33, the spiral traveling direction of the spiral current collecting member 43 as shown in FIGS. It is desirable that the shape as seen from is a drum shape.
[0042]
The drum-shaped spiral current collecting member 43 is formed on a substantially flat surface 43a that comes into contact with the fuel cell 33 and a non-contact portion 43b that keeps electrical and physical connection between the fuel cells 33. The bent portion 43c is formed.
[0043]
The bent portion 43c generates elasticity in the direction between the fuel cells 33, and when the distance between the fuel cells 33 is reduced, the bent portion 43c moves inside the spiral current collecting member 43. There is no interference or contact with the adjacent spiral current collecting member 43 or the adjacent fuel cell 33, and the reliability of the electrical connection can be improved.
[0044]
As shown in FIG. 4, the contact portion 43a of the spiral current collecting member 43 has corrugated unevenness, and a concave portion 43a1 formed in the contact portion 43a is formed in the gas flow direction. In FIG. 4, the direction perpendicular to the paper surface is the gas flow direction. The gas passes between the concave portion 43a1 formed in the contact portion 43a of the spiral current collecting member 43 and the outer surface of the oxygen-side electrode 33d, and the supply of the oxygen-containing gas to the surface of the oxygen-side electrode 33d can be increased. Performance can be improved.
[0045]
A plurality of spiral current collecting members 43 are arranged between the opposed fuel cells 33. By arranging a plurality of fuel cells, the current collection resistance between the fuel cells 33 can be reduced, and the current collection characteristics between the fuel cells 33 can be improved.
[0046]
Further, the spiral current collecting member 43 is disposed between the interconnector 33e which is a flat portion of the opposed fuel cell 33 and the oxygen-side electrode 33d, and the fuel cells 33 are connected in series. Since the contact portion 43a of the spiral current collecting member 43 is in contact with the flat portion of the fuel cell 33, the contact can be reliably made and the electrical connection can be reliably made.
[0047]
A portion of the contact portion 43a protruding toward the fuel cell 33 is joined to the oxygen-side electrode 33d and the interconnector 33e of the fuel cell 33 via a conductive paste 44, for example, an Ag paste. This Ag paste is baked, for example, at the time of power generation, and the contact portion 43a is joined to the interconnector 33e and the oxygen-side electrode 33d of the fuel cell 33, whereby the spiral current collector 43 and the fuel cell 33 are connected. A sufficient electrical connection can be obtained.
[0048]
Note that the entire surface of the contact portion 43a contacts the interconnector 33e, and the portion of the contact portion 43a protruding toward the oxygen electrode 33d may be contacted with the oxygen electrode 33d as described above. In this case, the connection and fixing of the contact portion 43a can be performed more reliably.
[0049]
A plurality of these spiral current collecting members 43 are interposed between the opposed fuel cells 33, and these spiral current collecting members 43 are made of a ferritic stainless steel mainly composed of conductive Cr and Fe. The surface is coated with an oxidation-resistant substance made of Ag. Note that the spiral current collecting member 43 is not limited to the above as long as it has a conductive metal or alloy as a main component and its surface is coated with an oxidation-resistant substance.
[0050]
In the fuel cell of the present invention, the spiral current collecting member 43 has a spring property, for example, because the abutting portion 43a having an elliptical cross section or an angular contact is in surface contact with the outer surface of the fuel cell 33. The area in contact with the fuel cell 33 is larger than that of the conventional felt-shaped current collecting member, and the current collecting characteristics can be improved. Further, the spiral current collecting member 43 has a large elastic force, and can secure a sufficient contact with the fuel cell 33 for a long period even if vibration or the like occurs. Further, in particular, by forming irregularities in the contact portion 43a and passing the fuel gas between the spiral current collecting member 43 and the outer surface of the fuel cell 33, the fuel gas can be sufficiently supplied to the solid electrolyte 33b, Power generation characteristics can be improved.
[0051]
Further, since the spiral current collecting member 43 is linear, even when the temperature inside the storage container 31 becomes high, the spiral current collecting member 43 is less likely to sinter than the conventional felt-shaped current collecting member. Sufficient contact can be secured for a long time.
[0052]
In the fuel cell configured as described above, an oxygen-containing gas (for example, air) from the outside is introduced into the heat exchanger 41a via the oxygen-containing gas pipe 73, and is introduced into the oxygen-containing gas storage chamber 41b. A fuel gas (for example, hydrogen) is supplied to the fuel gas flow path of the fuel cell 33 via the fuel gas supply pipe 51 while causing the fuel gas to be ejected between the fuel cells 33 via the content gas supply pipe 39 to generate electric power.
[0053]
Excess fuel gas not used for power generation gushes into the combustion space 37 from the upper end of the fuel gas flow path, and excess oxygen-containing gas not used for power generation flows into the combustion space 37, and surplus fuel gas and The excess oxygen-containing gas is reacted and burned to generate combustion gas, which is led out to the heat exchanger 41a via the combustion gas inlet 71 and discharged from the upper end of the heat exchanger 41a.
[0054]
Excess fuel gas and oxygen-containing gas that have not contributed to power generation are introduced into the combustion space 37, react and burn in the combustion space 37, and the combustion gas and external oxygen-containing gas are exchanged by the heat exchanger. The heat is exchanged between the combustion gas and the oxygen-containing gas by the heat exchanger 41a, so that the oxygen-containing gas can be preheated at the time of start-up. The insertion allows the oxygen-containing gas in the oxygen-containing gas supply pipe 39 to be further heated by the combustion gas, so that the fuel cell 33 is indirectly heated by the heated oxygen-containing gas to substantially generate power. Start-up time can be reduced.
[0055]
Furthermore, since the combustion space 37, the oxygen-containing gas storage chamber 41b, and the heat exchanger 41a are formed adjacent to each other at the upper part of the cell stack 35, the high-temperature combustion gas burned in the combustion space 37 can be piped. The preheating efficiency of the oxygen-containing gas can be increased with a simple structure.
[0056]
Further, since the combustion gas and the oxygen-containing gas can be heat-exchanged in the storage container 31, there is no need to separately provide a burner for preheating the oxygen-containing gas in the storage container 31, and the combustion gas can be reduced in size. Can be used effectively.
[0057]
Further, since the oxygen-containing gas storage chamber 41b is provided in the heat exchanger 41a, the connection between the heat exchanger 41a and the oxygen-containing gas supply pipe 39 can be performed through the oxygen-containing gas storage chamber 41b. The oxygen-containing gas from 41a can be reliably supplied into the power generation space 75.
[0058]
Note that the present invention is not limited to the above-described embodiment, and various changes can be made without changing the gist of the present invention. For example, in the above embodiment, the description has been given using the fuel cell 33 having a plurality of flat fuel gas channels 34 as shown in FIG. 2. However, the fuel cell 33 has one fuel gas channel 34. The shape of the fuel cell 33 is not particularly limited.
[0059]
In some cases, a plurality of spiral current collecting members 43 are arranged between the fuel cells 33. In this case, for example, the spiral current collecting members 43 are combined to form, for example, a raft shape. Thus, the spiral current collecting member 43 can be easily arranged.
[0060]
Further, in the above example, the example in which the fuel cells 33 are connected in series has been described. However, the fuel cell using the wide spiral current collecting member 43 in which a plurality of such spiral current collecting members 43 are combined is used. Assembling becomes easier by connecting a plurality of cells 33 in parallel.
[0061]
Further, although the fuel-side electrode 33b is an inner electrode, the oxygen-side electrode 33d may be an inner electrode.
[0062]
Further, the case where the fuel gas is supplied to the fuel cells 33 using one fuel gas tank 45 has been described. However, in the present invention, the fuel gas tanks 45 are provided for each row of the fuel cells 33, and the fuel cell A burner for directly heating the cell 33 may be provided. In this case, the fuel cell 33 can be directly heated by the burner at the time of startup, and the startup can be performed more quickly.
[0063]
【The invention's effect】
In the cell stack of the present invention, the current collecting member has a spiral shape, and is in contact with the outer surface of the opposed fuel cell. Since the spiral current collecting member has spring properties, the current collecting member is in surface contact with the outer surface of the fuel cell. In addition to being able to improve the current collecting characteristics, the spiral shape of the current collecting member has a large elastic force, and can ensure sufficient contact with the fuel cell for a long period of time. And sufficient contact with the fuel cells can be ensured for a long period of time.
[Brief description of the drawings]
FIG. 1 is an explanatory view showing a fuel cell of the present invention.
FIG. 2 is a cross-sectional view showing the cell stack of FIG.
3A and 3B show a state in which fuel cells are connected using a spiral current collecting member and a shape of the spiral current collecting member. FIG. 3A is a side view of the spiral current collecting member viewed from the side. (B) is a plan view of the spiral current collecting member used in (a) as viewed from the gas flow direction, (c) is a side view of another type of spiral current collecting member viewed from the side, and (d) is a side view thereof. It is the top view which looked at the spiral current collection member used at (c) from the gas flow direction.
FIG. 4 is an explanatory diagram showing a connection structure between a fuel cell and a spiral current collector.
[Explanation of symbols]
31 ... storage container 33 ... fuel cell 33a ... support 33b ... fuel side electrode (inside electrode)
33c: solid electrolyte 33d: oxygen side electrode (outer electrode)
33e Interconnector 34 Gas flow path 35 Cell stack 43 Spiral current collecting member 43a Contact portions (both ends)
43a1... Recess of the contact portion

Claims (10)

燃料電池セル間をガスが流通するセルスタックであって、前記燃料電池セル間に、線状部材を螺旋状に巻回してなる螺旋状集電部材を配置し、対向する前記燃料電池セル同士を電気的に接続してなることを特徴とするセルスタック。A cell stack in which gas flows between fuel cells, wherein a spiral current collecting member formed by spirally winding a linear member is disposed between the fuel cells, and the opposing fuel cells are separated from each other. A cell stack characterized by being electrically connected. 螺旋状集電部材が、螺旋進行方向から見て鼓形状であり、螺旋状集電部材の略平坦部が燃料電池セルと当接してなることを特徴とする請求項1記載のセルスタック。2. The cell stack according to claim 1, wherein the spiral current collecting member has a drum shape when viewed from the spiral traveling direction, and a substantially flat portion of the spiral current collecting member is in contact with the fuel cell. 螺旋状集電部材がガス流通方向に向けて螺旋状に形成されていることを特徴とする請求項1又は2記載のセルスタック。3. The cell stack according to claim 1, wherein the spiral current collecting member is spirally formed in the gas flowing direction. 螺旋状集電部材の燃料電池セル外面との当接部には凹凸が形成されていることを特徴とする請求項1乃至3のうちいずれかに記載のセルスタック。The cell stack according to any one of claims 1 to 3, wherein an uneven portion is formed at a contact portion of the spiral current collector with the outer surface of the fuel cell. 螺旋状集電部材の燃料電池セル外面との当接部には波形の凹凸が形成されており、前記螺旋状集電部材の当接部に形成された凹部がガス流通方向に形成されていることを特徴とする請求項1乃至4のうちいずれかに記載のセルスタック。Corrugations are formed at the contact portion of the spiral current collecting member with the outer surface of the fuel cell, and the concave portion formed at the contact portion of the spiral current collecting member is formed in the gas flow direction. The cell stack according to any one of claims 1 to 4, wherein: 燃料電池セルは、軸長方向にガス流路が形成された支持体の表面に、内側電極、固体電解質、外側電極を順次形成し、前記固体電解質及び前記外側電極が形成されていない支持体又にインターコネクタを設けてなり、一方の燃料電池セルのインターコネクタと他方の燃料電池セルの外側電極に、螺旋状集電部材が当接していることを特徴とする請求項1乃至5のうちいずれかに記載のセルスタック。The fuel cell has a structure in which an inner electrode, a solid electrolyte, and an outer electrode are sequentially formed on the surface of a support having a gas flow path formed in the axial direction, and the solid electrolyte and the outer electrode are not formed on the support or The spiral current collector is in contact with the interconnector of one fuel cell and the outer electrode of the other fuel cell. The cell stack described in Crab. 燃料電池セルは、酸素含有ガスに曝される外側電極を有しており、螺旋状集電部材が、導電性を有する金属又は合金の表面を耐酸化性物質で被覆して構成されていることを特徴とする請求項1乃至6のうちいずれかに記載のセルスタック。The fuel cell has an outer electrode exposed to an oxygen-containing gas, and the spiral current collector is configured by coating a conductive metal or alloy surface with an oxidation-resistant substance. The cell stack according to claim 1, wherein: 螺旋状集電部材の燃料電池セル外面との当接部は、導電性ペーストにより対向する燃料電池セルの外面に接合されていることを特徴とする請求項1乃至7のうちいずれかに記載のセルスタック。The abutting portion of the spiral current collector with the outer surface of the fuel cell is joined to the outer surface of the opposed fuel cell by a conductive paste, according to any one of the preceding claims. Cell stack. 燃料電池セルは扁平状であり、対向する燃料電池セルの外面は略平坦であることを特徴とする請求項1乃至8のうちいずれかに記載のセルスタック。9. The cell stack according to claim 1, wherein the fuel cells have a flat shape, and the outer surfaces of the opposed fuel cells are substantially flat. 収納容器内に、請求項1乃至9のうちいずれかに記載のセルスタックを収納してなることを特徴とする燃料電池。A fuel cell comprising the cell stack according to any one of claims 1 to 9 stored in a storage container.
JP2003018010A 2003-01-27 2003-01-27 Cell stack and fuel cell Expired - Fee Related JP3898647B2 (en)

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JP2006210056A (en) * 2005-01-26 2006-08-10 Kyocera Corp End part current collector member and fuel battery cell stack using this, fuel cell
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JP2007035498A (en) * 2005-07-28 2007-02-08 Kyocera Corp Current collection structure in fuel battery cell stack
JP2007227203A (en) * 2006-02-24 2007-09-06 Kyocera Corp Fuel cell stack and power collecting member
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JP2015118854A (en) * 2013-12-19 2015-06-25 京セラ株式会社 Cell stack device, fuel cell module and fuel cell device
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JP2007227203A (en) * 2006-02-24 2007-09-06 Kyocera Corp Fuel cell stack and power collecting member
JP2013030358A (en) * 2011-07-28 2013-02-07 Kyocera Corp Cell stack and fuel cell module
JP2013219020A (en) * 2012-04-06 2013-10-24 Korea Inst Of Energy Research Flat-tubular solid oxide unit cell, and flat-tubular solid oxide fuel cell and flat-tubular solid oxide electrolyzer including the same
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JP2014127427A (en) * 2012-12-27 2014-07-07 Kyocera Corp Collector member, cell stack device and fuel cell
JP2015118854A (en) * 2013-12-19 2015-06-25 京セラ株式会社 Cell stack device, fuel cell module and fuel cell device
JP2017016740A (en) * 2015-06-26 2017-01-19 京セラ株式会社 Cell stack, module and module housing device
JP2017033631A (en) * 2015-07-28 2017-02-09 アイシン精機株式会社 Solid oxide type fuel battery stack, solid oxide type fuel battery module and solid oxide type fuel battery system

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